Multiple catalyst system for olefin polymerization and polymers produced therefrom

ABSTRACT

This invention relates to a polymer comprising one or more C3 to C40 olefins, optionally one or more diolefins, and less than 15 mole % of ethylene, where the polymer has: a) a Dot T-Peel of 1 Newton or more; and b) a branching index (g′) of 0.95 or less measured at the Mz of the polymer; c) an Mw of 100,000 or less. This invention also relates a polymer comprising one or more C3 to C40 olefins where the polymer has: a) a Dot T-Peel of 1 Newton or more on Kraft paper; b) a branching index (g′) of 0.95 or less measured at the Mz of the polymer; c) a Mw of 10,000 to 100,000; and d) a heat of fusion of 1 to 70 J/g. This invention also relates a polymer comprising one or more C3 to C40 olefins where the polymer has: a) a Dot T-Peel of 1 Newton or more on Kraft paper; b) a branching index (g′) of 0.98 or less measured at the Mz of the polymer; c) a Mw of 10,000 to 60,000; d) a heat of fusion of 1 to 50 J/g. This invention also relates to a homopolypropylene or a copolymer of propylene and up to 5 mole % ethylene having: a) an isotactic run length of 1 to 30 (isotactic run length “IRL” is defined to be the percent of mmmm pentad divided by 0.5× percent of mmmr pentad) as determined by Carbon 13 NMR, preferably 3 to 25, more preferably 4 to 20, b) a percent of r dyad of greater than 20%, preferably from 20 to 70% as determined by Carbon 13 NMR, and c) a heat of fusion of 70 J/g or less, preferably 60 J/g or less, more preferably between 1 and 55 J/g, more preferably between 4 and 50 J/g. This invention further relates to a process to produce an olefin polymer comprising: 1) selecting a first catalyst component capable of producing a polymer having an Mw of 100,000 or less and a crystallinity of 5% or less at selected polymerization conditions; 2) selecting a second catalyst component capable of producing polymer having an Mw of 100,000 or less and a crystallinity of 20% or more at the selected polymerization conditions; 3) contacting the catalyst components in the presence of one or more activators with one or more C3 to C40 olefins, at the selected polymerization conditions in a reaction zone; 4) obtaining the polymer. This invention further relates to a continuous process to produce a branched olefin polymer comprising: 1) selecting a first catalyst component capable of producing a polymer having an Mw of 100,000 or less and a crystallinity of 5% or less under selected polymerization conditions; 2) selecting a second catalyst component capable of producing polymer having an Mw of 100,000 or less and a crystallinity of 20% or more at the selected polymerization conditions; 3) contacting the catalyst components in the presence of one or more activators with one or more C3 to C40 olefins, and, optionally one or more diolefins; 4) at a temperature of greater than 100° C.; 5) at a residence time of 120 minutes or less; 6) wherein the ratio of the first catalyst to the second catalyst is from 1:1 to 50:1; 7) wherein the activity of the catalyst components is at least 100 kilograms of polymer per gram of the catalyst components; and wherein at least 20% of the olefins are converted to polymer.

RELATED CASE INFORMATION

This application is a divisional of U.S. Ser. No. 10/687,508, filed Oct.15, 2003 which claims priority to provisional U.S. Ser. No. 60/418,482,filed Oct. 15, 2002, and also claims priority from U.S. Ser. No.60/460,714, filed Apr. 4, 2003.

This application is related to U.S. Ser. No. 60/199,093, filed on Apr.21, 2000 and US2000000199093P, filed Apr. 20, 2001 claiming priorityfrom U.S. Ser. No. 60/199,093. The instant application also relates toU.S. Ser. No. 60/171,715, filed Dec. 21, 1999; U.S. Ser. No. 09/745,394,filed Dec. 21, 2000; and U.S. Ser. No. 09/746,332 filed Dec. 21, 2000.The instant application also relates to WO 01/81493.

FIELD OF THE INVENTION

This invention relates to a process to polymerize olefins using multiplecatalysts and polymers produced therefrom. In particular this inventionrelates to a process to produce polyolefin adhesives and the adhesivesso produced.

BACKGROUND OF THE INVENTION

For some applications such as adhesives individual polymers do notpossess the necessary combination of properties. Individual polyolefinshaving certain characteristics are often blended together in the hope ofcombining the positive attributes of the individual components.Typically the result is a blend which displays an average of theindividual properties of the individual resins. For example EP 0 527 589discloses blends of flexible, low molecular weight amorphouspolypropylene with higher molecular weight isotactic polypropylene toobtain compositions with balanced mechanical strength and flexibility.These compositions show better flexibility compared to that of theisotactic polypropylene alone, but are still lacking in other physicalattributes. Physical blends also have the problems of inadequatemiscibility. Unless the components are selected for their compatibilitythey can phase separate or smaller components can migrate to thesurface. Reactor blinds, also called intimate blends (a compositioncomprising two or more polymers made in the same reactor or in a seriesof reactors) are often used to address these issues, however findingcatalyst systems that will operate under the same environments toproduce different polymers has been a challenge.

Multiple catalyst systems have been used in the past to produce reactorblends (also called intimate blends) of various polymers and otherpolymer compositions. Reactor blends and other one-pot polymercompositions are often regarded as superior to physical blends ofsimilar polymers. For example U.S. Pat. No. 6,248,832 discloses apolymer composition produced in the presence of one or morestereospecific metallocene catalyst systems and at least onenonstereospecific metallocene catalyst system. The resultant polymer hasadvantageous properties over the physical blends disclosed in EP 0 527589 and U.S. Pat. No. 5,539,056.

Thus there has been interest in the art in developing multiple catalystsystems to produce new polymer compositions. For example, U.S. Pat. No.5,516,848 discloses the use of two different cyclopentadienyl basedtransition metal compounds activated with alumoxane or non-coordinatinganions. In particular, the examples disclose, among other things,catalyst compounds in combination, such as(Me₂Si(Me₄C₅)(N-c-C₁₂H₂₃)TiCl₂ and rac-Me₂Si(H₄Ind)ZrCl₂, orMe₂Si(Me₄C₅)(N-c-C₁₂H₂₃)TiCl₂ and Me₂Si(Ind₂)HfMe₂, (Ind=indenyl)activated with activators such as methylalumoxane or N,N-dimethylanilinium tetrakis(pentafluorphenyl)borate to produce polypropyleneshaving bimodal molecular weight distributions (Mw/Mn), varying amountsof isotacticity (from 12 to 52 weight % isotactic PP in the product inEx 2, 3 and 4), and having weight average molecular weights over100,000, and some even as high as 1,200,000 for use as thermoplastics.Likewise, U.S. Pat. No. 6,184,327 discloses a thermoplastic elastomercomprising a branched olefin polymer having crystalline sidechains andan amorphous backbone wherein at least 90 mole percent of the sidechainsare isotactic or syndiotactic polypropylene and at least 80 mole percentof the backbone is atactic polypropylene produced by a processcomprising: a) contacting, in solution, at a temperature from about 90°C. to about 120° C., propylene monomers with a catalyst compositioncomprising a chiral, stereorigid transition metal catalyst compoundcapable of producing isotactic or syndiotactic polypropylene; b)copolymerizing the product of a) with propylene and, optionally, one ormore copolymerizable monomers, in a polymerization reactor using anachiral transition metal catalyst capable of producing atacticpolypropylene; and c) recovering a branched olefin polymer. SimilarlyU.S. Pat. No. 6,147,180 discloses the synthesis of a thermoplasticpolymer composition, which is produced by first polymerizing monomers toproduce at least 40% vinyl terminated macromonomers and thencopolymerizing the macromonomers with ethylene. In addition U.S. Pat.No. 6,323,284 discloses a method to produce thermoplastic compositions(mixtures of crystalline and amorphous polyolefin copolymers) bycopolymerizing alpha-olefins and alpha, omega dienes using two separatecatalyst systems.

Likewise others have experimented with multiple stage processes toproduce new polymer compositions. For example EP 0 366 411 discloses agraft polymer having an EPDM backbone with polypropylene grafted theretoat one or more of the diene monomer sites through the use of a two-stepprocess using a different Ziegler-Natta catalyst system in each step.This graft polymer is stated to be useful for improving the impactproperties in blended polypropylene compositions.

Although each of the polymers described in the above references hasinteresting combinations of properties, there remains a need for newcomposition that offer other new and different property balancestailored for a variety of end uses. In particular, it would be desirableto find a composition that is strong yet has adhesive characteristicsand the ability to be applied using adhesive technology and equipment.

For general information in this area, one may refer to:

-   1. DeSouza and Casagrande, in 2001 addressed the issue of binary    catalyst systems in “Recent Advances in Olefin Polymerization Using    Binary Catalyst Systems, Macromol. Rapid Commun. 2001, 22, No. 16    (pages 1293 to 1301). At page 1299 they report propylene systems    that produce a “gooey” product.-   2. Studies with respect to the production of stereoblock    polypropylene by using in-situ mixtures of metallocene catalysts    with different stereoselectivity were recently performed by Lieber    and Brintzinger in “Propene Polymerization with Catalyst Mixtures    Containing Different Ansa-Zirconocenes: Chain Transfer to    Alkylaluminum Cocatalysts and Formation of Stereoblock Polymers”,    Macromolecules 2000, 33, No. 25 (pages 9192-9199). Propylene    polymerization reactions were performed using metallocene catalysts    H₄C₂(Flu)₂ZrCl₂, rac-Me₂Si(2-Me-4-tBu-C₅H₂)₂ZrCl₂ and    rac-Me₂Si(2-MeInd)₂ZrCl₂ in the presence of either MAO    (methylalumoxane) or triisobutylaluminium    (Al^(i)Bu₃)/triphenylcarbenium    tetrakis(perfluorophenylborate)(trityl borate) as the cocatalyst.    Propylene polymerization using the mixed catalysts, H₄C₂(Flu)₂ZrCl₂    and rac-Me₂Si(2-MeInd)₂ZrCl₂ in the presence of either MAO or    AliBu₃/trityl borate produced waxy solids, which are completely    separable into an atactic (diethyl ether-soluble) and an isotactic    (insoluble) fraction. Neither fraction contained any combination of    isotactic and atactic pentad patterns indicating that these catalyst    mixtures did not form stereoblock polymers.-   3. Aggarwal addressed the various polymers produced in “Structures    and Properties of Block Polymers and Multiphase Polymer Systems: An    Overview of Present Status and Future Potential”, S. L. Aggarwal,    Sixth Biennial Manchester Polymer Symposium (UMIST Manchester, March    1976)-   4. “Selectivity in Propene Polymerization with Metallocene    Catalysts” Resconi, et al, Chem Rev. 2000, 100, 1253-1345.

None of the references above has directly addressed the need forpolyolefin based adhesives containing both amorphous and crystallinecomponents. Such adhesives are desired in the industry as a replacementfor blends requiring significant amount of hydrocarbon resin tackifiers.

Additional references that are of interest include:

-   1) EP Patents: EP 0619325 BI, EP 719802 B1;-   2) US Patents/Publications: U.S. Pat. Nos. 6,207,606, 6,258,903;    6,271,323; 6,340,703, 6,297,301, US 2001/0007896 A1, U.S. Pat. Nos.    6,184,327, 6,225,432, 6,342,574, 6,147,180, 6,114,457, 6,143,846,    5,998,547; 5,696,045; 5,350,817, U.S. Pat. No. 6,569,965,-   3) PCT Publications: WO 00/37514, WO 01/81493, WO 98/49229, WO    98/32784; and WO 01/09200-   4) “Metallocene-Based Branch-Block thermoplastic Elastomers,”    Markel, et al. Macromolecules 2000, Volume 33, No. 23. pgs.    8541-8548.

SUMMARY OF THE INVENTION

This invention relates to a polymer comprising one or more C3 to C40olefins, optionally one or more diolefins, and less than 15 mole % ofethylene, where the polymer has:

-   -   a) a Dot T-Peel of 1 Newton or more; and    -   b) a branching index (g′) of 0.95 or less measured at the Mz of        the polymer;    -   c) an Mw of 100,000 or less.

This invention also relates to a polymer comprising one or more C3 toC40 olefins where the polymer has:

-   -   a) a Dot T-Peel of 1 Newton or more on Kraft paper;    -   b) a branching index (g′) of 0.95 or less measured at the Mz of        the polymer;    -   c) a Mw of 10,000 to 100,000; and    -   d) a heat of fusion of 1 to 70 J/g.

This invention also relates a polymer comprising one or more C3 to C40olefins where the polymer has:

-   -   a) a Dot T-Peel of 1 Newton or more on Kraft paper;    -   b) a branching index (g′) of 0.98 or less measured at the Mz of        the polymer;    -   c) a Mw of 10,000 to 60,000;    -   d) a heat of fusion of 1 to 50 J/g.

This invention also relates to a homopolypropylene or a copolymer ofpropylene and up to 5 mole % ethylene having:

-   -   a) an isotactic run length of 1 to 30 (isotactic run length        “IRL” is defined to be the percent of mmmm pentad divided by        0.5× percent of mmmr pentad) as determined by Carbon 13 NMR,        preferably 3 to 25, more preferably 4 to 20,    -   b) a percent of r dyad of greater than 20%, preferably from 20        to 70% as determined by Carbon 13 NMR, and    -   c) a heat of fusion of 70 J/g or less, preferably 60 J/g or        less, more preferably between 1 and 55 J/g, more preferably        between 4 and 50 J/g.

This invention further relates to a process to produce an olefin polymercomprising:

-   -   1) selecting a first catalyst component capable of producing a        polymer having an Mw of 100,000 or less and a crystallinity of        5% or less at selected polymerization conditions;    -   2) selecting a second catalyst component capable of producing        polymer having an Mw of 100,000 or less and a crystallinity of        20% or more at the selected polymerization conditions;    -   3) contacting the catalyst components in the presence of one or        more activators with one or more C3 to C40 olefins, at the        selected polymerization conditions in a reaction zone;    -   4) obtaining the polymer.

This invention further relates to a continuous process to produce abranched olefin polymer comprising:

-   -   1) selecting a first catalyst component capable of producing a        polymer having an Mw of 100,000 or less and a crystallinity of        5% or less under selected polymerization conditions;    -   2) selecting a second catalyst component capable of producing        polymer having an Mw of 100,000 or less and a crystallinity of        20% or more at the selected polymerization conditions;    -   3) contacting the catalyst components in the presence of one or        more activators with one or more C3 to C40 olefins, and,        optionally one or more diolefins;    -   4) at a temperature of greater than 100° C.;    -   5) at a residence time of 120 minutes or less;    -   6) wherein the ratio of the first catalyst to the second        catalyst is from 1:1 to 50:1;    -   7) wherein the activity of the catalyst components is at least        100 kilograms of polymer per gram of the catalyst components;        and wherein at least 20% of the olefins are converted to        polymer.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is an illustration of complex viscosity changes with thetemperature when the samples were cooled at 10 C per minute for Examples12, 22 and 49.

FIG. 2 is a graphic illustration of the relationship between thebranching index, g′, and the molecular weight for polymers produced inExamples 4 and 31.

FIG. 3 is the C-13 NMR spectra of heptane soxhlet insoluble (top trace)and hexane room temperature soluble fractions (bottom trace) extractedfrom Example 4.

FIG. 4 is the C-13 NMR spectra of aPP/scPP branch block relative to scPPand aPP control. The control samples were produced using one catalyst ata time; aPP was synthesized using a specific catalyst, while the scPPwas produced using stereospecific catalyst. The top trace is the aPPcontrol sample. The middle trace is the scPP control sample and thebottom trace is Example 4.

FIG. 5 shows the relationship between temperature and complex viscosityof the fractionated samples extracted from example 31.

FIG. 6 is the DSC trace for polymer of example 32 in Table 6.

DETAILED DESCRIPTION

For the purposes of this; invention and the claims thereto and for easeof reference when a polymer is referred to as comprising an olefin, theolefin present in the polymer is the polymerized form of the olefin.

In another embodiment this invention relates to a polymer comprising oneor more C3 to C40 olefins, preferably propylene, and less than 50 mole %of ethylene, having:

-   -   a) a Dot T-Peel between 1 Newton and the 10,000 Newtons; and    -   b) a Mz/Mn of 2 to 200; and/or

c) an Mw of X and a g′ of Y (measured at the Mz of the polymer)according to the following Table C: TABLE C X (Mw) Y (g′) 100,000 orless, preferably 80,000 or less, preferably 70,000 or less, more 0.9 orless, preferably 60,000 or less, more preferably 50,000 or less, morepreferably preferably 0.7 or 40,000 or less, more preferably 30,000 orless, more preferably 20,000 or less, less more preferably 10,000 orless. In some embodiments X is also at least 7000, Preferably morepreferably 10,000, more preferably at least 15,000. between 0.5-0.975,000 or less, preferably 70,000 or less, more preferably 60,000 orless, more 0.92 or less, preferably 50,000 or less, more preferably40,000 or less, more preferably preferably, 0.6 or 30,000 or less, morepreferably 20,000 or less, more preferably 10,000 or less. less In someembodiments A is also at least 1000, preferably at least 2000, morepreferably between preferably at least 3000, more preferably at least4000, more preferably at 0.4-0.6- least 5000, more preferably at least7000, more preferably 10,000, more preferably at least 15,000. 50,000 orless, more preferably 40,000 or less, more preferably 30,000 or less,0.95 or less, more preferably 20,000 or less, more preferably 10,000 orless. In some preferably 0.7 or embodiments A is also at least 1000,preferably at least 2000, more preferably less at least 3000, morepreferably at least 4000, more preferably at least 5000, preferablybetween more preferably at least 7000, more preferably 10,000, morepreferably at 0.5-0.7- least 15,000. 30,000 or less, preferably 25,000or less, more preferably 20,000 or less, more 0.98 or less preferably15,000 or less, more preferably 10,000 or less. In some preferablybetween embodiments A is also at least 1000, preferably at least 2000,more preferably 0.7-0.98 at least 3000, more preferably at least 4000,more preferably at least 5000, more preferably at least 7000, morepreferably 10,000, more preferably at least 15,000.

In another embodiment, when Mw is between 15,000 and 100,000, theng′<(10¹²Mw²-10⁻⁶Mw+1.0178).

In a some embodiments the g′ is 0.9 or less, 0.8 or less, 0.7 or less,0.6 or less, 0.5 or less measured at the Mz of the polymer.

In another embodiment the polymer described above also has a peakmelting point (Tm) between 40 and 250° C., or between 60 and 190° C., orbetween about 60 and 150° C., or between 80 and 130° C. In someembodiments the peak melting point is between 60 arid 160° C. In otherembodiments the peak melting point is between 124-140° C. In otherembodiments the peak melting temperature is between 40-130° C.

In another embodiment the polymer described above also has a viscosity(also referred to a Brookfield Viscosity or Melt Viscosity) of 90,000mPa·sec or less at 190° C. (as measured by ASTM D 3236 at 190° C.); or80,000 or less, or 70,000 or less, or 60,000 or less, or 50,000 or less,or 40,000 or less, or 30,000 or less, or 20,000 or less, or 10,000 orless, or 8,000 or less, or 5000 or less, or 4000 or less, or 3000 orless, or 1500 or less, or between 250 and 6000 mPa·sec, or between 500and 5500 mPa·sec, or between 500 and 3000 mPa·sec, or between 500 and1500 mPa·sec, and/or a viscosity of 8000 mPa·sec or less at 160° C. (asmeasured by ASTM D 3236 at 160° C.); or 7000 or less, or 6000 or less,or 5000 or less, or 4000 or less, or 3000 or less, or 1500 or less, orbetween 250 and 6000 mPa·sec, or between 500 and 5500 mPa·sec, orbetween 500 and 3000 mPa·sec, or between 500 and 1500 mPa·sec. In otherembodiments the viscosity is 200,000 mPa·sec or less at 190 ° C.,depending on the application. In other embodiments the viscosity is50,000 mPa·sec or less depending on the applications.

In another embodiment the polymer described above also has a heat offusion of 70 J/g or less, or 60 J/g oar less, or 50 J/g or less; or 40J/g or less, or 30 J/g or less, or 20 J/g or less and greater than zero,or greater than 1 J/g, or greater than 10 J/g, or between 20 and 50 J/g.

In another embodiment the polymer described above also has a Shore AHardness (as measured by ASTM 2240) of 95 or less, 70 or less, or 60 orless, or 50 or less, or 40 or less or 30 or less, or 20 or less. Inother embodiments the Shore A Hardness is 5 or more, 10 or more, or 15or more. In certain applications, such as packaging, the Shore AHardness is preferably 60-70.

In another embodiment the polymer of this invention has an Mz/Mn of 2 to200, preferably 2 to 150, preferably 10 to 100.

In another embodiment the polymer described above also has a ShearAdhesion Fail Temperature (SAFT—as measured by ASTM 4498) of 200° C. orless, or of 40 to 150° C., or 60 to 130° C., or 65 to 110° C., or 70-80°C. In certain embodiments SAFT's of 130-140° C. are preferred.

In another embodiment the polymer described above also has a Dot T-Peelof between 1 Newton and 10,000 Newtons, or 3 and 4000 Newtons, orbetween 5 and 3000 Newtons, or between 10 and 2000 Newtons, or between15 and 1000 Newtons. Dot T-Peel is determined according to ASTM D 1876,except that the specimen is produced by combining two 1 inch by 3 inch(2.54 cm×7.62 cm) Kraft paper substrate cut outs with a dot of adhesivewith a volume that, when compressed under a 500 gram weight occupiesabout 1 square inch of area (1 inch=2.54 cm). Once made all thespecimens are pulled apart in side by side testing (at a rate of 2inches per minute) by a machine that records the destructive force ofthe insult being applied. The maximum force achieved for each sampletested was recorded and averaged, thus producing the Average MaximumForce which is reported as the Dot T-Peel.

In another embodiment the polymer described above also has a set time ofseveral days to 1 second, or 60 seconds or less, or 30 seconds or less,or 20 seconds or less, or 15 seconds or less, or 10 seconds or less, or5 seconds or less, or 4 seconds or less, or 3 seconds or less, more or 2seconds or less, or 1 second or less.

In another embodiment the polymer described above also has an Mw/Mn of 2to 75, or 4 to 60, or 5 to 50, or 6 to 20.

In another embodiment the polymer described above also has an Mz of1,000,000 or less, preferably 15,000 to 1,000,000, or 20,000 to 800,000,or 25,000 to 350,000.

In another embodiment the polymer described above may also have a strainat break (as measured by ASTM D-1708 at 25 ° C.) of 50 to 1000%,preferably 80 to 200%. In some other embodiments the strain at break is100 to 500%.

In another embodiment, the polymer described herein has a tensilestrength at break (as measured by ASTM D-1708 at 25 ° C.) of 0.5 MPa ormore, alternatively 0.75 MPa or more, alternatively 1.0 MPa or more,alternatively 1.5 MPa or more, alternatively 2.0 MPa or more,alternatively 2.5 MPa or more, alternatively 3.0 MPa or more,alternatively 3.5 MPa or more.

In another embodiment the polymer described above also has acrystallization point (Tc) between 20 and 110° C. In some embodimentsthe Tc is between 70 to 100° C. In other embodiments the Tc is between30 to 80° C. In other embodiments the Tc is between 20 to 50° C.

In some embodiments the polymers described above have a slope of −0.1 orless, preferably −0.15 or less;, more preferably −0.25 or less in thetrace of complex viscosity versus temperature as shown in FIG. 1 (asmeasured by ARES dynamic mechanical spectrometer operating at afrequency of 10 rad/s, with a strain of 20% under a nitrogen atmosphere,and a cooling rate of 10° C./min) over the range of temperatures fromTc+10° C. to Tc+40° C. The slope is defined as a derivative of log(complex viscosity) with respect to temperature.

In another embodiment the polymer described above has a Tc that is atleast 10° C. below the Tm, preferably at least 20° C. below the Tm,preferably at least 30° C. below the Tm, more preferably at least 35° C.below the Tm.

In another embodiment some polymers described above have a melt indexratio (I₁₀/I₂) of 6.5 or less, preferably 6.0 or less, preferably 5.5 orless, preferably 5.0 or less, preferably 4.5 or less, preferably between1 and 6.0. (I₁₀ and I₂ are measured according to ASTM 1238 D, 2.16 kg,190° C.).

In another embodiment some polymers described above have a melt index(as determined by ASTM 1238 D, 2.16 kg, 190 deg. C) of 25 dg/min ormore, preferably 50 dg/min or more, preferably 100 dg/min or more, morepreferably 200 dg/min or more, more preferably 500 dg/mn or more, morepreferably 2000 dg/min or more.

In another embodiment the polymer has a melt index of 900 dg/min ormore.

In another embodiment the polymer described above has a range ofcrystallization of 10 to 60° C. wide, preferably 20 to 50° C.,preferably 30 to 45° C. in the DSC traces. In DSC traces where there aretwo or more non-overlapping peaks, then each peak has a range ofcrystallization of 10 to 60° C. wide, preferably 20 to 50° C.,preferably 30 to 45° C. in the DSC traces.

In another embodiment the polymer produced by this invention has amolecular weight distribution (Mw/Mn) of at least 2, preferably at least5, preferably at least 10, even more preferably at least 20.

In another embodiment the polymer produced may have a unimodal, bimodal,or multimodal molecular weight distribution (Mw/Mn) distribution ofpolymer species as determined by Size Exclusion Chromatography (SEC). Bybimodal or multimodal is meant that the SEC trace has more than one peakor inflection points. An inflection point is that point where the secondderivative of the curve changes in sign (e.g., from negative to positiveor vice versus).

In another embodiment the polymer described above has an Energy ofactivation of 8 to 15 cal/mol. Energy of activation was calculated usingthe relationships of complex viscosity and temperature over the regionwhere thermal effects are responsible for viscosity increase (assumingan Arrhenius-like relationship).

In another embodiment the polymers of this invention may have acrystallinity of at least 5%.

In another embodiment the polymer described above may also have one ormore of the following:

-   -   a) a peak melting point between 60 and 190° C., or between about        60 and 150° C., or between 80 and 130° C.; and/or    -   b) a viscosity of 8000 mPa·sec or less at 190° C. (as measured        by ASTM D 3236 at 190° C.); or 5000 or less, or 4000 or less, or        3000 or less, or 1500 or less, or between 250 and 6000 mPa·sec,        or between 500 and 5500 mPa·sec, or between 500 and 3000        mPa·sec, or between 500 and 1500 mPa·sec, or a viscosity of 8000        mPa·sec or less at 160° C. (as measured by ASTM D 3236 at 160°        C.); or 7000 or less, or 6000 or less, or 5000 or less, or 4000        or less, or 3000 or less, or 1500 or less, or between 250 and        6000 mPa·sec, or between 500 and 5500 mPa·sec, or between 500        and 3000 mPa·sec, or between 500 and 1500 mPa·sec; and/or    -   c) an H_(f) (Heat of fusion) of 70 J/g or less, or 60 J/g or        less, or 50 J/g or less; or 40 J/g or less, or 30 J/g or less,        or 20 J/g or less and greater than zero, or greater than 1 J/g,        or greater than 10 J/g, or between 20 and 50 J/g; and or    -   d) a Shore A Hardness (as measured by ASTM 2240) of 90 or less,        or 80 or less, or 70 or less, or 60 or less or 50 or less, or 40        or less; and or    -   e) a Shear Adhesion Fail Temperature (SAFT—as measured by        ASTM 4498) of 40 to 150° C., or 60 to 130° C., or 65 to 110° C.,        or 70-80° C.; and or;    -   f) a Dot T-Peel of between 1 Newton and 10,000 Newtons , or 3        and 4000 Newtons, or between 5 and 3000 Newtons, or between 10        and 2000 Newtons, or between 15 and 1000 Newtons; and/or    -   g) a set time of several days to 0.1 second, or 60 seconds or        less, or 30 seconds or less, or 20 seconds or less, or 15        seconds or less, or 10 seconds or less, or 5 seconds or less, or        4 seconds or less, or 3 seconds or less, more or 2 seconds or        less, or 1 second or less; and or    -   h) an Mw/Mn of greater than 1 to 75, or 2 to 60, or 2 to 50, or        3 to 20; and/or    -   i) an Mz of 1,000,000 or less, preferably 15,000 to 500,000, or        20,000 to 400,000, or 25,000 to 350,000.

Useful combinations of features include polymers as described abovehaving a Dot T-Peel of between 1 Newton and 10,000 Newtons , or 3 and4000 Newtons, or between 5 and 3000 Newtons, or between 10 and 2000Newtons, or between 15 and 1000 Newtons and:

-   1. an Mw of 30,000 or less, a peak melting point between 60 and 190°    C., a Heat of fusion of 1 to 70 J/g, a branching index (g′) of 0.90    or less measured at the Mz of the polymer; and a melt viscosity of    8000 mPa·sec or less at 190° C.; or-   2. an Mz of 20,000 to 500,000 and a SAFT of 60 to 150° C.; or-   3. an Mz/Mn of 2-200 and a set time of 2 seconds or less; or-   4. an Hf (heat of fusion) of 20 to 50 J/g, an Mz or 20,000-500,000    and a shore hardness of 50 or less; or-   5. an Mw/Mn of greater than 1 to 50, a viscosity of 5000 or less    mPa·sec at 190° C.; or-   6. an Mw of 50,000 or less, a peak melting point between 60 and 190°    C., a heat of fusion of 2 to 70 J/g, a branching index (g′) of 0.70    or less measured at the Mz of the polymer, and a melt viscosity of    8000 mPa·sec or less at 190° C.

In a preferred embodiment, the polymer of this invention comprisesamorphous, crystalline and branch-bloc k molecular structures.

In a preferred embodiment the polymer comprises at least 50 weight %propylene, preferably at least 60% propylene, alternatively at least 70%propylene, alternatively at least 80% propylene. In another embodimentthe polymer comprises propylene and 15 mole % ethylene or less,preferably 10 mole % ethylene or less, more preferably 9 mole % ethyleneor less, more preferably 8 mole % ethylene or less, more preferably 7mole % ethylene or less, more preferably 6 mole % ethylene or less, morepreferably 5 mole % ethylene or less, more preferably 4 mole % ethyleneor less, more preferably 3 mole % ethylene or less, more preferably 2mole % ethylene or less, more preferably 1 mole % ethylene or less.

In another embodiment the polymer of this invention comprises less than5 mole % of ethylene, preferably less than 4.5 mole % ethylene,preferably less than 4.0 mole % ethylene, alternatively less than 3.5mole % ethylene, alternatively less than 3.0 mole % ethylene,alternatively less than 2.5 mole % ethylene, alternatively less than 2.0mole % ethylene, alternatively less than 1.5 mole % ethylene,alternatively less than 1.0 mole % ethylene, alternatively less than 0.5mole % ethylene, alternatively less than 0.25 mole % ethylene,alternatively 0 mole % ethylene.

In another embodiment the polymer produced has a glass transitiontemperature (Tg) as measured by ASTM E 1356 of 5° C. or less, preferably0° C. or less, preferably −5 ° C. or less, alternatively between −5° C.and −40° C., alternatively between −5 ° C. and −15° C.

In another embodiment the polymer of this invention has an amorphouscontent of at least 50%, alternatively at least 60%, alternatively atleast 70%, even alternatively between 50 and 99%. Percent amorphouscontent is determined using Differential Scanning Calorimetrymeasurement according to ASTM E 794-85.

In another embodiment the polymer of this invention has a crystallinityof 40% or less, alternatively 30% or less, alternatively 20% or less,even alternatively between 10% and 30%. Percent crystallinity content isdetermined using Differential Scanning Calorimetry measurement accordingto ASTM E 794-85. In another embodiment, the polymers described hereinhave a percent crystallinity of between 5 and 40%, alternatively between10 to 30%.

In another embodiment the polymer produced by this invention has amolecular weight distribution (Mw/Mn) of at least 1.5, preferably atleast 2, preferably at least 5, preferably at least 10, evenalternatively at least 20. In other embodiments the Mw/Mn is 20 or less,10 or less, even 5 or less. Molecular weight distribution generallydepends on the catalysts used and process conditions such astemperature, monomer concentration, catalyst ratio, if multiplecatalysts are used, and the presence or absence of hydrogen. Hydrogenmay be used at amounts up to 2 weight %, but is preferably used atlevels of 50 to 500 ppm.

In another embodiment the polymer produced is found to have at least twomolecular weights fractions are present at greater than 2 weight %,preferably greater than 20 weight %, each based upon the weight of thepolymer as measured by Gel Permeation Chromatography. The fractions canbe identified on the GPC trace by observing two distinct populations ofmolecular weights. An example would be a GPC trace showing a peak at20,000 Mw and another peak at 50,000 Mw where the area under the firstpeak represents more than 2 weight % of the polymer and the area underthe second peak represents more than 2 weight % of the polymer.

In another embodiment the polymer of this invention has 20 weight % ormore (based upon the weight of the starting polymer) of hexane roomtemperature soluble fraction, and 70 weight % or less, preferably 50weight % or less of Soxhlet boiling heptane insolubles, based upon theweight of the polymer. Soxhlet heptane insoluble refers to one of thefractions obtained when a sample is fractionated using successivesolvent extraction technique. The fractionations are carried out in twosteps: one involves room temperature solvent extraction, the othersoxhlet extraction. In the room temperature solvent extraction, aboutone gram of polymer is dissolved in 50 ml of solvent (e.g., hexane) toisolate the amorphous or very low molecular weight polymer species. Themixture is stirred at room temperature for about 12 hours. The solublefraction is separated from the insoluble material using filtration undervacuum. The insoluble material is then subjected to a Soxhlet extractionprocedure. This involves the separation of polymer fractions based ontheir solubility in various solvents having boiling points from justabove room temperature to 110° C. The insoluble material from the roomtemperature solvent extraction is first extracted overnight with asolvent such as hexane and heptane (Soxhlet); the extracted material isrecovered by evaporating the solvent and weighing the residue. Theinsoluble sample is then extracted with a solvent having higher boilingtemperature such as heptane and after solvent evaporation, it isweighed. The insolubles and the thimble from the final stage areair-dried in a hood to evaporate most of the solvent, then dried in anitrogen-purged vacuum oven. The amount of insoluble left in the thimbleis then calculated, provided the tare weight of the thimble is known.

In another embodiment, the polymers produced in this invention have aheptane insoluble fraction 70 weight % or less, based upon the weight ofthe starting polymer, and the heptane insoluble fraction has branchingindex g′ of 0.9 (preferably 0.7) or less as measured at the Mz of thepolymer. In a preferred embodiment the composition also has at least 20weight % hexane soluble fraction, based upon the weight of the startingpolymer. In another embodiment, the polymers produced in this inventionhave a heptane insoluble fraction 70 weight % or less, based upon theweight of the starting polymer and a Mz between 20,000 and 5000,000 ofthe heptane insoluble portion. In a preferred embodiment the compositionalso has at least 20 weight % hexane soluble fraction, based upon theweight of the starting polymer. In another embodiment the polymersproduced have a hexane soluble portion of at least 20 weight %, basedupon the weight of the starting polymer.

In another embodiment the polymer comprises propylene and 15 mole %ethylene or less, preferably 10 mole % ethylene or less, more preferably9 mole % ethylene or less, more preferably 8 mole % ethylene or less,more preferably 7 mole % ethylene or less, more preferably 6 mole %ethylene or less, more preferably 5 mole % ethylene or less, morepreferably 4 mole % ethylene or less, more preferably 3 mole % ethyleneor less, more preferably 2 mole % ethylene or less, more preferably 1mole % ethylene or less.

In another embodiment the polymer of this invention comprises less than5 mole % of ethylene, preferably less than 4.5 mole % ethylene,preferably less than 4.0 mole % ethylene, alternatively less than 3.5mole % ethylene, alternatively less than 3.0 mole % ethylene,alternatively less than 2.5 mole % ethylene, alternatively less than 2.0mole % ethylene, alternatively less than 1.5 mole % ethylene,alternatively less than 1.0 mole % ethylene, alternatively less than 0.5mole % ethylene, alternatively less than 0.25 mole % ethylene,alternatively 0 mole % ethylene.

For ease of reference the polymer produced by the second catalyst havingat least 20% crystallinity may also be referred to as the“semi-crystalline polymer” and the polymer produced by the firstcatalyst component having a crystallinity of less than 5% may bereferred to as the “amorphous polymer.”

In another embodiment of this invention the polymer produced has acharacteristic three-zone complex viscosity-temperature pattern, asshown in FIG. 1. The temperature dependence of complex viscosity wasmeasured using ARES dynamic mechanical spectrometer operating at afrequency of 10 rad/s, with a strain of 20% under a nitrogen atmosphere,and a cooling rate of 10° C./min. The sample was first molten thengradually cooled down to room temperature while monitoring the build-upin complex viscosity. Above the melting point, which is typical ofpolymer processing temperature, the complex viscosity is relatively low(Zone I) and increases gradually with decreasing temperature. In zoneII, a sharp increase in complex viscosity appears as temperature isdropped. The third zone (Zone III) is the high complex viscosity zone,which appears at lower temperatures corresponding to application (enduse) temperatures. In Zone III the complex viscosity is high and variesslightly with further decrease in temperature. Such a complex viscosityprofile provides, in hot melt adhesive applications, a desirablecombination of long opening time at processing temperatures and fast settime at lower temperatures.

In a preferred embodiment, the polymers produced herein having less than1 mol % ethylene, have at least 2 mol % (CH₂)₂ units, preferably 4 mol%, preferably 6 mol %, more preferably 8 mol %, more preferably 10 mol%, more preferably 12 mol %, more preferably 15 mol %, more preferably18 mol %, more preferably 5 mol % as measured by Carbon 13 NMR asdescribed below.

In an another embodiment, the polymers produced herein having between 1and 10 mol % ethylene, have at least 2+X mol % (CH₂)₂ units, preferably4+X mol %, preferably 6+X mol %, more preferably 8+X mol %, morepreferably 10+X mol %, more preferably 12+X mol %, more preferably 15+Xmol %, more preferably 18+X mol %, more preferably 20+X mol %, where Xis the mole % of ethylene, and the (CH₂)₂ units are determined by Carbon13 NMR as described below.

In a preferred embodiment, the polymers produced herein, having lessthan 1 mol % ethylene, have an amorphous component (which is defined tobe that portion of the polymer composition that has a crystallinity ofless than 5%) which contains at least 3 mol % (CH₂)₂ units, preferably 4mol %, preferably 6 mol %, more preferably 8 mol %, more preferably 10mol %, more preferably 12 mol %, more preferably 15 mol %, morepreferably 18 mol %, more preferably 20 mol % as measured by Carbon 13NMR as described below.

In an another embodiment, the polymers produced herein having between 1and 10 mol % ethylene, have an amorphous component (which is defined tobe that portion of the polymer composition that has a crystallinity ofless than 20%) which contains at least 3+X mol % (CH₂)₂ units,preferably 4+X mol %, preferably 6+X mol %, more preferably 8+X mol %,more preferably 10+X mol %, more preferably 12+X mol %, more preferably15+X mol %, more preferably 18+X mol %, more preferably 20+X mol %,where X is the mole % of ethylene, and the (CH₂)₂ units are determinedby Carbon 13 NMR as described below.

Monomers

In a preferred embodiment the polymer comprises an olefin homopolymer orcopolymer, comprising one or more C3 to C40 alpha olefins. In anotherpreferred embodiment the olefin polymer further comprises one or morediolefin comonomers, preferably one or more C4 to C40 diolefins.

In a preferred embodiment the polymer comprises an olefin homopolymer orcopolymer, having less than 5 mol % ethylene, and comprising one or moreC3 to C40 alpha olefins. In another preferred embodiment the olefinpolymer, having less than 5 mol % ethylene, further comprises one ormore diolefin comonomers, preferably one or more C4 to C40 diolefins.

In a preferred embodiment the polymer produced herein is a propylenehomopolymer or copolymer. The comonomer is preferably a C4 to C20linear, branched or cyclic monomer, and in one embodiment is a C4 to C12linear or branched alpha-olefin, preferably butene, pentene, hexene,heptene, octene, nonene, decene, dodecene, 4-methyl-pentene-1,3-methylpentene-1, 3,5,5-trimethyl-hexene-1, and the like. Ethylene may bepresent at 5 mol % or less.

In another embodiment the polymer produced herein is a copolymer of oneor more linear or branched C3 to C30 prochiral alpha-olefins or C5 toC30 ring containing olefins or combinations thereof capable of beingpolymerized by either stereospecific and non-stereospecific catalysts.Prochiral, as used herein, refers to monomers that favor the formationof isotactic or syndiotactic polymer when polymerized usingstereospecific catalyst(s).

The polymerizable olefinic moiety can be linear, branched,cyclic-containing, or a mixture of these structures. Preferred linearalpha-olefins include C3 to C8 alpha-olefins, more preferalblypropylene, 1-butene, 1-hexene, and 1-octene, even more preferablypropylene or 1-butene. Preferred branched alpha-olefins include4-methyl-1-pentene, 3-methyl-1-pentene, and 3,5,5-trimethyl-1-hexene,5-ethyl-1-nonene. Preferred aromatic-group-containing monomers containup to 30 carbon atoms. Suitable aromatic-group-containing monomerscomprise at least one aromatic structure, preferably from one to three,more preferably a phenyl, indenyl, fluorenyl, or naphthyl moiety. Thearomatic-group-containing monomer further comprises at least onepolymerizable double bond such that after polymerization, the aromaticstructure will be pendant from the polymer backbone. The aromatic-groupcontaining monomer may further be substituted with one or morehydrocarbyl groups including but not limited to C1 to C10 alkyl groups.Additionally two adjacent substitutions may be joined to form a ringstructure. Preferred aromatic-group-containing monomers contain at leastone aromatic structure appended to a polymerizable olefinic moiety.Particularly preferred aromatic monomers include styrene,alpha-methylstyrene, para-alkylstyrenes, vinyltoluenes,vinylnaphthalene, allyl benzene, and indene, especially styrene,paramethyl styrene, 4-phenyl-1-butene and allyl benzene.

Non aromatic cyclic group containing monomers are also preferred. Thesemonomers can contain up to 30 carbon atoms. Suitable non-aromatic cyclicgroup containing monomers preferably have at least one polymerizableolefinic group that is either pendant on the cyclic structure or is partof the cyclic structure. The cyclic structure may also be furthersubstituted by one or more hydrocarbyl groups such as, but not limitedto, C1 to C 10 alkyl groups. Preferred non-aromatic cyclic groupcontaining monomers include vinylcyclohexane, vinylcyclohexene,vinylnorbornene, ethylidene norbornene, cyclopentadiene, cyclopentene,cyclohexene, cyclobutene, vinyladamantane and the like.

Preferred diolefin monomers useful in this invention include anyhydrocarbon structure, preferably C4 to C30, having at least twounsaturated bonds, wherein at least two of the unsaturated bonds arereadily incorporated into a polymer by either a stereospecific or anon-stereospecific catalyst(s). It is further preferred that thediolefin monomers be selected from alpha, omega-diene monomers (i.e.,di-vinyl monomers). More preferably, the diolefin monomers are lineardi-vinyl monomers, most preferably those containing from 4 to 30 carbonatoms. Examples of preferred dienes include butadiene, pentadiene,hexadiene, heptadiene, octadiene, nonadiene, decadiene, undecadiene,dodecadiene, tridecadiene, tetradecadiene, pentadecadiene,hexadecadiene, heptadecadiene, octadecadiene, nonadecadiene, icosadiene,heneicosadiene, docosadiene, tricosadiene, tetracosadiene,pentacosadiene, hexacosadiene, heptacosadiene, octacosadiene,nonacosadiene, triacontadiene, particularly preferred dienes include1,6-heptadiene, 1,7-octadiene, 1,8-nonadiene, 1,9-decadiene,1,10-undecadiene, 1,11-dodecadiene, 1,12-tridecadiene,1,13-tetradecadiene, and low molecular weight polybutadienes (Mw lessthan 1000 g/mol). Preferred cyclic dienes include cyclopentadiene,vinylnorbornene, norbornadiene, ethylidene norbornene, divinylbenzene,dicyclopentadiene or higher ring containing diolefins with or withoutsubstituents at various ring positions.

In a preferred embodiment one or more dienes are present in the polymerproduced herein at up to 10 weight %, preferably at 0.00001 to 1.0weight %, preferably 0.002 to 0.5 weight %, even more preferably 0.003to 0.2 weight %, based upon the total weight of the composition. In someembodiments 500 ppm or less of diene is added to the polymerization,preferably 400 ppm or less, preferably or 300 ppm or less. In otherembodiments at least 50 ppm of diene is added to the polymerization, or100 ppm or more, or 150 ppm or more.

In a preferred embodiment the olefin polymer is homopolypropylene. Inanother preferred embodiment the olefin polymer comprises propylene,ethylene, preferably less than 5 mol % ethylene, and at least onedivinely comonomer. In another preferred embodiment the olefin polymercomprises propylene and at least one divinely comonomer.

In another embodiment, the olefin polymer comprises:

-   -   a first monomer present at from 40 to 95 mole %, preferably 50        to 90 mole %, preferably 60 to 80 mole %, and    -   a comonomer present at from 5 to 40 mole %, preferably 10 to 60        mole %, more preferably 20 to 40 mole %,and    -   a termonomer present at from 0 to 10 mole %, more preferably        from 0.5 to 5 mole %, more preferably 1 to 3 mole %.

In a preferred embodiment the first monomer comprises one or more of anyC3 to C8 linear, branched or cyclic alpha-olefins, including propylene,butene (and all isomers thereof), pentene (and all isomers thereof),hexene (and all isomers thereof), heptene (and all isomers thereof), andoctene (and all isomers thereof). Preferred monomers include propylene,1-butene, 1-hexene, 1-octene, and the like.

In a preferred embodiment the comonomer comprises one or more of any C2to C40 linear, branched or cyclic alpha-olefins (provided ethylene, ifpresent, is present at 5 mole % or less), including ethylene, propylene,butene, pentene, hexene, heptene, and octene, nonene, decene, undecene,dodecene, hexadecene, styrene,3,5,5-trimethylhexene-1,3-methylpentene-1,4-methylpentene-1, norborneneand cyclopentene.

In a preferred embodiment the termonomer comprises one or more of any C2to C40 linear, branched or cyclic alpha-olefins, (preferably ethylene,if present, is present at 5 mole % or less), including, but not limitedto, ethylene, propylene, butene, pentene, hexene, heptene, and octene,nonene, decene, undecene, dodecene, hexadecene, butadiene,1,5-hexadiene, 1,6-heptadiene, 1,4- pentadiene, 1,7-octadiene,1,8-nonadiene, 1,9-decadiene, 1,11-dodecadiene, styrene,3,5,5-trimethylhexene-1,3-methylpentene-1,4-methylpentene-1, andcyclopentadiene.

In a preferred embodiment the polymer comprises propylene and from 0 to50 mole % ethylene, preferably from 0 to 30 mole % ethylene, morepreferably from 0 to 15 mole % ethylene, more preferably from 0 to 10mole % ethylene, more preferably from 0 to 5 mole % ethylene.

In a preferred embodiment the polymer comprises propylene and from 0 to50 mole % butene, preferably from 0 to 30 mole % butene, more preferablyfrom 0 to 15 mole % butene, more preferably from 0 to 10 mole % butene,more preferably from 0 to 5 mole % butene.

In a preferred embodiment the polymer comprises propylene and from 0 to50 mole % hexene, preferably from 0 to 30 mole % hexene, more preferablyfrom 0 to 15 mole % hexene, more preferably from 0 to 10 mole % hexene,more preferably from 0 to 5 mole % hexene.

Process

This invention further relates to a process to produce the olefinpolymers described above comprising:

-   -   1) selecting a first catalyst (component capable of producing a        polymer having an Mw of 100,000 or less and a heat of fusion of        10 J/g or less;    -   2) selecting a second catalyst component capable of producing        polymer having an Mw of 100,000 or less and a crystallinity of        20% or more;    -   3) contacting the catalyst components in the presence of one or        more activators with one or more olefins, in a reaction zone.

This invention further relates to a process to produce the olefinpolymers described above comprising:

-   -   1) selecting a first catalyst component capable of producing a        polymer having an Mw of 100,000 or less and a heat of fusion of        10 J/g or less;    -   2) selecting a second catalyst component capable of producing        polymer having an Mw of 100,000 or less and a crystallinity of        20% or more;    -   3) contacting the catalyst components in the presence of one or        more activators with one or more olefins and one or more dienes,        in a reaction zone.

This invention further relates to a process to produce the olefinpolymers described above comprising:

-   -   1) selecting a first catalyst component capable of producing a        polymer having an Mw of 100,000 or less and a heat of fusion of        70 J/g or less, capable of polymerizing macromonomers having        reactive termini;    -   2) selecting a second catalyst component capable of producing        macromonomers having reactive termini, an Mw of 100,000 or less        and a crystallinity of 30% or more;    -   3) contacting the catalyst components in the presence of one or        more activators with one or more olefins, and optionally a        diolefin in a reaction zone.

This invention further relates to a process to produce the olefinpolymers described above comprising:

-   -   1) selecting a first catalyst component capable of producing a        polymer having an Mw of 30,000 or less and a heat of fusion of        10 J/g or less, capable of polymerizing macromonomers having        reactive termini;    -   2) selecting a second catalyst component capable of producing        macromonomers having reactive termini, an Mw of 30,000 or less        and a crystallinity of 20% or more;    -   3) contacting the catalyst components in the presence of one or        more activators with propylene, and optionally other olefins, in        a reaction zone

In another preferred embodiment this invention relates to a continuousprocess to produce a branched olefin polymer comprising:

-   -   1) selecting a first catalyst component capable of producing a        polymer having an Mw of 100,000 or less, preferably 80,000 or        less, preferably 60,000 or less and a crystallinity of 5% or        less, preferably 3% or less, more preferably 2% or less, under        selected polymerization conditions;    -   2) selecting a second catalyst component capable of producing        polymer having an Mw of 100,000 or less, preferably 80,000 or        less, preferably 60,000 or less and a crystallinity of 20% or        more, preferably 30% or more, more preferably 40% or more at the        selected polymerization conditions;    -   3) contacting, under the selected polymerization conditions, the        catalyst components in the presence of one or more activators        with one or more C3 to C40 olefins, preferably one or more C3 to        C12 olefins, preferably C3 and one or more of ethylene and/or C4        to C20 comonomers, and, optionally one or more diolefins,        preferably a C4 to C20 diene;    -   4) at a temperature of greater than 70 ° C., preferably greater        than 100° C., preferably greater than 105° C., more preferably        greater than 110° C., more preferably greater than 115° C.;    -   5) at a residence time of 120 minutes or less, preferably 60        minutes or less, preferably 50 minutes or less, preferably 40        minutes, preferably 30 minutes or less, preferably 25 minutes or        less, more preferably 20 minutes or less, more preferably 15        minutes or less, more preferably at 10 minutes or less, more        preferably at 5 minutes or less, more preferably at 3 minutes or        less, alternately the residence time may be between 60 and 120        minutes;    -   6) wherein the ratio of the first catalyst to the second        catalyst is from 1:1 to 50:1, preferably 1:1 to 20:1, more        preferably 1:1 to 1:10;    -   7) wherein the activity of the catalyst components is at least 3        kilograms, preferably at least 50 kilograms, more preferably at        least 100 kilograms, more preferably at least 200 kilograms,        more preferably, 300 kilograms, more preferably 400 kilograms,        more preferably 500 kilograms of polymer per gram of the        catalyst mixture; and wherein at least 80%, preferably at least        85%, more preferably at least 90%, more preferably at least 95%        of the olefins are converted to polymer.

In another embodiment the a first catalyst component is capable ofproducing a polymer having an Mw of 100,000 or less and a crystallinityof 5% or less at selected polymerization conditions and the secondcatalyst component is capable of producing polymer having an Mw of100,000 or less and a crystallinity of 20% or more at the selectedpolymerization conditions.

In another embodiment at least 20% or more of the olefins are convertedto polymer, preferably 20% or more, more preferably 60% or more, morepreferably 75% or more, more preferably 85% or more, more preferably 95%or more.

In a preferred embodiment the process described above takes place in asolution phase, slurry or bulk phase polymerization process.

By continuous is meant a system that operates (or is intended tooperate) without interruption or cessation. For example a continuousprocess to produce a polymer would be one where the reactants arecontinually introduced into one or more reactors and polymer product iscontinually withdrawn.

In another preferred embodiment, in the process described above theconcentrations of the reactants vary by 20% or less in the reaction zoneduring the residence time, preferably by 15% or less, more preferably by10% or less. In a preferred embodiment the concentration of themonomer(s) remains constant in the reaction zone during the residencetime. Preferably the concentration of the monomer(s) varies by 20% orless, preferably by 15% or less, more preferably by 10% or less, morepreferably by 5% or less.

In a preferred embodiment the concentration of the catalyst componentsremains constant in the reaction zone during the residence time.Preferably the concentration of the monomer(s) varies by 20% or less,preferably by 15% or less, more preferably by 10% or less, morepreferably by 5% or less.

In a preferred embodiment the concentration of the activator(s) remainsconstant in the reaction zone during the residence time. Preferably theconcentration of the monomer(s) varies by 20% or less, preferably by 15%or less, more preferably by 10% or less, more preferably by 5% or less.

In another preferred embodiment a third catalyst (or more) may bepresent in the processes described above. The third catalyst may be anyof the catalyst components listed herein. Preferred third catalystsinclude catalysts that are capable of producing waxes. Other preferredthird catalysts may include any catalyst described herein. One mayselect two or more catalysts to produce various macromonomers havingreactive termini, used in combination with a catalyst that canpolymerize such macromonomers. One may select two or more catalysts thatcan polymerize macromonomers and one catalyst that can producemacromonomers with reactive termini. Likewise one could also selectthree catalysts that produce different polymers under the same reactionconditions. For example one could select a catalyst that produces asomewhat crystalline polymer, one that produces a very crystallinepolymer and one that produces an amorphous polymer, any of which mayproduce macromonomers with reactive termini or polymerize polymershaving reactive termini. Similarly one could select two catalysts, onethat produces crystalline polymers and one that produces an amorphouspolymer, any of which may make macromonomers with reactive termini orpolymerize polymers having reactive termini. Likewise one could select acatalyst that produces a somewhat crystalline polymer, one that producesa wax and one that produces an amorphous polymer, any of which may makemacromonomers with reactive termini or polymerize polymers havingreactive termini.

By reaction zone is meant an area where the activated catalyst andmonomers can react.

By macromonomers having reactive termini is meant a polymer havingtwelve or more carbon atoms (preferably 20 or more, more preferably 30or more, more preferably between 12 and 8000 carbon atoms) and having avinyl, vinylidene, vinylene or other terminal group that can bepolymerized into a growing polymer chain. By capable of polymerizingmacromonomer having reactive termini is meant a catalyst component thatcan incorporate a macromonomer (which tend to be molecules larger than atypical single monomer such as ethylene or propylene), having reactivetermini into a growing polymer chain. Vinyl terminated chains aregenerally more reactive than vinylene or vinylidene terminated chains.

In a particular embodiment the present invention is directed to apolyolefin polymer produced by copolymerizing one or more C₃ or higheralpha-olefins and/or one or more di-vinyl monomers, and optionally up to5 mol % ethylene, in the presence of at least one stereospecificcatalyst system and at least one other catalyst system in the samepolymerization medium. Preferably, the polymerizations are carried outsimultaneously in the presence of both catalysts. The polymer soproduced may contain amorphous polymer segments and crystalline polymersegments in which at least some of the segments are linked. Typicallythe amorphous and the crystalline polymer segments are copolymers of oneor more alpha-olefins (optionally including up to 5 mol % ethylene)and/or one or more monomers having at least two olefinically unsaturatedbonds. Both of these unsaturated bonds are suitable fir and readilyincorporated into a growing polymer chain by coordination polymerizationusing either the first or second catalyst systems independently suchthat the di-olefin is incorporated into polymer segments produced byboth catalysts in the mixed catalyst system according to this invention.In a preferred embodiment these monomers having at least twoolefinically unsaturated bonds are di-olefins, preferably di-vinylmonomers. Crosslinking of at least a portion of the mixture of polymersegments is believed to be accomplished during the polymerization of thecomposition by incorporation of a portion of di-vinyl comonomers intotwo polymer segments, thus producing a crosslink between those segments.

In another embodiment, polyolefin branch-block compositions containingamorphous and semi-crystalline components may be prepared in a singlereactor to yield desired property balance. In particular, aPP-g-scPPbranch structures may be produced in-situ in a continuous solutionreactor using mixed catalysts and propylene as the preferred feed. Inone embodiment stereospecific bridged bis-indenyl group 4 catalysts canbe selected to produce semicrystalline PP macromonomers. (All referencesto the Periodic Table of the Elements are to the Table published inChemical and Engineering News, 63(5), 27, 1985.) A bridgedmono-cyclopentadienyl heteroatom group 4 catalyst can be used to buildamorphous PP (aPP) backbone while simultaneously incorporating some ofthe semi-crystalline macromonomers (scPP). This is believed to produce aaPP-g-scPP structure where the “-g-” indicates hat the polymer types areat least partially grafted. By selecting the catalysts, thepolymerization reaction conditions, and/or by introducing a dienemodifier, the amorphous and crystalline components can be linkedtogether to produce various branch-block structures. To effectivelyincorporate into a growing chain, a macromonomer with vinyl end group ispreferred. Other types of chain end unsaturations (vinylene andvinylidene) can also be used. While not wishing to be bound by theory,branch-block copolymer is believed to comprise an amorphous backbonehaving crystalline side chains originating from the scPP macromonomersand the sidechains are believed to be polypropylene macromonomers, whichcan be prepared under solution polymerization conditions with catalystssuitable for preparing either of isotactic or syndiotacticpolypropylene.

A preferred reaction process to produce polypropylene macromonomershaving high levels of terminal vinyl unsaturation is described in U.S.Pat. No. 6,117,962. Typically used catalysts are stereorigid, chiral orasymmetric, bridged metallocenes. See, for example, U.S. Pat. No.4,892,851, U.S. Pat. No. 5,017,714, U.S. Pat. No. 5,132,281, U.S. Pat.No. 5,296,434, U.S. Pat. No. 5,278,264, U.S. Pat. No. 5,304,614, U.S.Pat. No. 5,510,502, WO-A-(PCT/US92/10066) WO-A-93/19103, EP-A2-0 577581, EP-A1-0 578 838, and academic literature “The Influence of AromaticSubstituents on the Polymerization Behavior of Bridged ZirconoceneCatalysts”, Spaleck, W., et al., Organometallics 1994, 13, 954-963, and“ansa-Zirconocene Polymerization Catalysts with Annelated RingLigands-Effects on Catalytic Activity and Polymer Chain Lengths”,Brinzinger, H., et al, Organometallics 1994, 13, 964-970, and documentsreferred to therein.

In some embodiments, the first catalyst which comprises a stereorigidtransition metal pre-catalyst compound used to produce thesemi-crystalline polypropylene macromonomers of the present invention isselected from the group consisting of racemic bridgedbis(indenyl)zirconocenes or hafnocenes. In a another embodiment, thetransition metal pre-catalyst compound is a rac-dimethylsilyl-bridgedbis(indenyl)zirconocene or hafnocene. In another embodiment, thetransition metal pre-catalyst compound is rac-dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium or hafnium dichloride ordimethyl. In another preferred embodiment, the transition metal catalystis a rac-dimethylsilyl-bridged bis(indenyl)hafnocene such asrac-dimethylsilyl bis(indenyl)hafnium dimethyl or dichloride.

It is believed that the fraction of branch-block and the level ofbranching depend on the availability of macromonomers with unsaturatedchain end and macromonomer incorporation capability of the specificcatalyst. To increase the population of aPP-g-scPP branch-blockcomposition, one typically operates within a process window that favorsmacromonomer production and insertion. Such conditions have beendescribed in U.S. Pat. No. 6,117,962 and the journal article by W. Wenget al., Macromol. Rapid Commun., 2000, 21, 1103-1107 and are furtherillustrated by the examples therein.

It is also believed that the higher the population of vinyl terminatedscPP macromonomers the higher the probability of getting themincorporated into aPP backbone and therefore the higher the branch-blockpopulation.

To further increase the population of macromonomers having vinyl chainends diolefin monomers can be introduced into the reaction medium. Theresultant product is typically a blend comprised of isotacticpolypropylene segments, atactic polypropylene segments, and increasedpopulation of branch-block species resulting from the additionalcouplings brought about by the diolefin crosslinking agent.

Crosslinking typically refers to the connection of two polymer segmentsby incorporation of each double bond of a diolefin monomer into twodifferent polymer segments. The polymer segments so connected can be thesame or different, with respect to their crystallinity. Three or morepolymer segments may also be connected via incorporation of two or morediolefins in on polymer segment into two other polymer segments.

A consideration for selection of the monomer, or combinations ofmonomers, is that, both crystalline and amorphous polymer segments canbe formed with the selection of two or more different catalyst systems.In some embodiments it is further desired that the level ofincorporation of the diolefin monomer, if present, into the crystallinesegments be limited to an amount that will not substantially alter itscrystallinity. The diolefin coupling agent is typically kept minimum toinsure the overall composition has a viscosity of 8000 mPa·s or less forsome adhesive applications.

As mentioned above, to increase the population of aPP-g-scPPbranch-block composition, one typically operates within a process windowthat favors macromonomer production and insertion. Favorable conditionsinclude:

-   -   1) High concentration of catalyst producing the semi-crystalline        vinyl terminated macromonomers, and or    -   2) Adjusting the Al/metal ratio; and or    -   3) High operating temperature; and or    -   4) Catalyst structure that has a high affinity for macromonomer        incorporation; and or    -   5) Relatively long residence time; and or    -   6) High monomer conversion (monomer starvation condition        enhances the insertion of macromonomer); and or    -   7) Addition of modifier (dione) to enhance the population of        vinyl terminated macromonomers.

Another method of enhancing aPP-g-scPP branch block compositions is toadd in a chain transfer agent that transfers a vinyl group to the end ofthe polymer chain while deactivating the catalyst. Such chain transferagents include, but are not limited to, vinyl chloride, vinyl fluoride,vinyl bromide. In the process, the catalyst is reactivated by thepresence of an aluminum alkyl activator such as an alumoxane (typicallymethylalumoxane).

Similarly, melting and crystallization characteristics can be controlledthrough catalyst selection, comonomer addition and changes in processconditions such as temperature and catalyst ratio if more than onecatalyst is used.

Catalyst Compounds

Any catalyst compound that can produce the desired polymer species maybe used in the practice of this invention. In the description herein thetransition metal compound may be described as a catalyst precursor, apre-catalyst compound or a catalyst compound, and these terms are usedinterchangeably. A catalyst system is combination of a catalystprecursor and an activator. Catalyst Compounds and Selection

Any pre-catalyst compound (catalyst precursor compound) that can producethe desired polymer species may be used in the practice of thisinvention. Pre-catalyst compounds which may be utilized in the processof the invention include metallocene transition metal compounds(containing one, two, or three cyclopentadienyl ligands per metal atom),non-metallocene early transition metal compounds (including those withamide and/or phenoxide type ligands), non-metallocene late transitionmetal compounds (including those with diimine or diiminepyridylligands), and other transition metal compounds.

Generally, bulky ligand metallocene compounds (pre-catalysts) useful inthis invention include half and full sandwich compounds having one ormore bulky ligands bonded to at least one metal atom. Typical bulkyligand metallocene compounds are generally described as containing oneor more bulky ligand(s) and one or more leaving group(s) bonded to atleast one metal atom. The bulky ligands are generally represented by oneor more open, acyclic, or fused ring(s) or ring system(s) or acombination thereof. These bulky ligands, preferably the ring(s) or ringsystem(s) are typically composed of atoms selected from Groups 13 to 16atoms of the Periodic Table of Elements, preferably the atoms areselected from the group consisting of carbon, nitrogen, oxygen, silicon,sulfur, phosphorous, germanium, boron and aluminum or a combinationthereof. Most preferably, the ring(s) or ring system(s) are composed ofcarbon atoms such as but not limited to those cyclopentadienyl ligandsor cyclopentadienyl-type ligand structures or other similar functioningligand structure such as a pentadienyl, a cyclooctatetraendiyl, acyclobutadienyl, or a substituted allyl ligand. Other ligands that canfunction similarly to a cyclopentadienyl-type ligand include amides,phosphides, imines, phosphinimines, amidinates, and ortho-substitutedphenoxides. The metal atom is preferably selected from Groups 3 through15 and or lanthanide or actinide series of the Periodic Table ofElements. Preferably the metal is a transition metal from Groups 3through 12, more preferably Groups 4, 5 and 6, and most preferably thetransition metal is from Group 4.

In one embodiment, the catalyst composition useful in the inventionincludes one or more bulky ligand metallocene catalyst compoundsrepresented by the formula:L^(A)L^(B)M^(Q)*_(n)  (1)where M is a metal atom from the Periodic Table of the Elements and maybe a Group 3 to 12 metal or from the lanthanide or actinide series ofthe Periodic Table of Elements, preferably M is a Group 4, 5 or 6transition metal, more preferably M is a Group 4 transition metal, evenmore preferably M is zirconium, hafnium or titanium. The bulky ligands,L^(A) and L^(B), are open, acyclic or fused ring(s) or ring system(s)and are any ancillary ligand system, including unsubstituted orsubstituted, cyclopentadienyl ligands or cyclopentadienyl-type ligands,heteroatom substituted and/or heteroatom containingcyclopentadienyl-type ligands. Non-limiting examples of bulky ligandsinclude cyclopentadienyl ligands, cyclopentaphenanthreneyl ligands,indenyl ligands, benzindenyl ligands, fluorenyl ligands,dibenzo[b,h]fluorenyl ligands, benzo[b]fluorenyl ligands,cyclooctatetraendiyl ligands, cyclopentacyclododecene ligands, azenylligands, azulene ligands, pentalene ligands, phosphoyl ligands,phosphinimine (WO 99/40125), pyrrolyl ligands, pyrozolyl ligands,carbazolyl ligands, boratobenzene ligands and the like, includinghydrogenated versions thereof, for example tetrahydroindenyl ligands. Inone embodiment, L^(A) and L^(B) may be any other ligand structurecapable of π-bonding to M. In yet another embodiment, the atomicmolecular weight (MW) of L^(A) or L^(B) exceeds 60 a.m.u., preferablygreater than 65 a.m.u. In another embodiment, L^(A) and L^(B) maycomprise one or more heteroatoms, for example, nitrogen, silicon, boron,germanium, sulfur and phosphorous, in combination with carbon atoms toform an open, acyclic, or preferably a fused, ring or ring system, forexample, a hetero-cyclopentadienyl ancillary ligand. Other L^(A) andL^(B) bulky ligands include but are not limited to bulky amides,phosphides, alkoxides, aryloxides, imides, carbolides, borollides,porphyrins, phthalocyanines, corrins and other polyazomacrocycles.Independently, each L^(A) and L^(B) may be the same or different type ofbulky ligand that is bonded to M. In one embodiment of Formula 1 onlyone of either L^(A) or L^(B) is present.

Independently, each L^(A) and L^(B) may be unsubstituted or substitutedwith a combination of substituent groups R*. Non-limiting examples ofsubstituent groups R* include one or more from the group selected fromhydrogen, or linear or branched alkyl radicals, alkenyl radicals,alkynyl radicals, cycloalkyl radicals, aryl radicals, acyl radicals,aroyl radicals, alkoxy radicals, aryloxy radicals, alkylthio radicals,dialkylamino radicals, alkoxycarbonyl radicals, aryloxycarbonylradicals, carbomoyl radicals, alkyl- or dialkyl-carbamoyl radicals,acyloxy radicals, acylamino radicals, aroylamino radicals or combinationthereof. In a preferred embodiment, substituent groups R* have up to 50non-hydrogen atoms, preferably from 1 to 30 carbon, that can also besubstituted with halogens or heteroatoms or the like. Non-limitingexamples of alkyl substituents R* include methyl, ethyl, propyl, butyl,pentyl, hexyl, cyclopentyl, cyclohexyl, benzyl or phenyl groups and thelike, including all their isomers, for example tertiary butyl,isopropyl, and the like. Other hydrocarbyl radicals includefluoromethyl, fluoroethyl, difluoroethyl, iodopropyl, bromohexyl,chlorobenzyl and hydrocarbyl substituted organometalloid radicalsincluding trimethylsilyl, trimethylgermyl, methyldiethylsilyl and thelike; and halocarbyl-substituted organometalloid radicals includingtris(trifluoromethyl)silyl, methyl-bis(difluoromethyl)silyl,bromomethyldimethylgermyl and the like; and disubstituted boron radicalsincluding dimethylboron for example; and disubstituted pnictogenradicals including dimethylamine, dimethylphosphine, diphenylamine,methylphenylphosphine, chalcogen radicals including methoxy, ethoxy,propoxy, phenoxy, methylsulfide and ethylsulfide. Non-hydrogensubstituents R* include the atoms carbon, silicon, boron, aluminum,nitrogen, phosphorous, oxygen, tin, sulfur, germanium and the like,including olefins such as but not limited to olefinically unsaturatedsubstituents including vinyl- terminated ligands, for examplebut-3-enyl, prop-2-enyl, hex-5-enyl and the like. Also, at least two R*groups, preferably two adjacent R groups, are joined to form a ringstructure having from 3 to 30 atoms selected from carbon, nitrogen,oxygen, phosphorous, silicon, germanium, aluminum, boron or acombination thereof. Also, a substituent group, R*, may also be adiradical bonded to L at one end and forming a carbon sigma bond to themetal M. Other ligands may be bonded to the metal M, such as at leastone leaving group Q*. In one embodiment, Q* is a monoanionic labileligand having a sigma-bond to M. Depending on the oxidation state of themetal, the value for n is 0, 1 or 2 such that Formula 1 above representsa neutral bulky ligand metallocene catalyst compound. Non-limitingexamples of Q* ligands include weak bases such as amines, phosphines,ethers, carboxylates, dienes, hydrocarbyl radicals having from 1 to 20carbon atoms, hydrides or halogens and the like or a combinationthereof. In another embodiment, two or more Q*'s form a part of a fusedring or ring system. Other examples of Q* ligands include thosesubstituents for R* as described above and including cyclobutyl,cyclohexyl, heptyl, tolyl, trifluoromethyl, tetramethylene (both Q*),pentamethylene (both Q*), methylidene (both Q*), methoxy, ethoxy,propoxy, phenoxy, bis(N-methylanilide), dimethylamide, dimethylphosphideradicals and the like.

In another embodiment, the catalyst composition useful in the inventionmay include one or more bulky ligand metallocene catalyst compoundswhere L^(A) and L^(B) of Formula 1 are bridged to each other by at leastone bridging group, A*, as represented by Formula 2.L^(A)A*L^(B)MQ*_(n)  (2)

The compounds of Formula 2 are known as bridged, bulky ligandmetallocene catalyst compounds. L^(A), L^(B), M, Q* and n are as definedabove. Nonlimiting examples of bridging group A.* include bridginggroups containing at least one Group 13 to 16 atom, often referred to asa divalent moiety such as but not limited to at least one of a carbon,oxygen, nitrogen, silicon, aluminum, boron, germanium and tin atom or acombination thereof. Preferably bridging group A* contains a carbon,silicon or germanium atom, most preferably A* contains at least onesilicon atom or at least one carbon atom. The bridging group A* may alsocontain substituent groups R* as defined above including halogens andiron. Non-limiting examples of bridging group A* may be represented byR′₂C, R′₂CCR′₂, R′₂Si, R′₂SiCR′₂, R′₂SiSiR′₂ R′₂Ge, R′P, R′N, R′B whereR′ is independently, a radical group which is hydride, hydrocarbyl,substituted hydrocarbyl, halocarbyl, substituted halocarbyl,hydrocarbyl-substituted organometalloid, halocarbyl-substitutedorganometalloid, disubstituted boron, disubstituted pnictogen,substituted chalcogen, or halogen or two or more R′ may be joined toform a ring or ring system. In one embodiment, the bridged, bulky ligandmetallocene catalyst compounds of Formula 2 have two or more bridginggroups A* (EP 664 301 B1). In another embodiment, the bulky ligandmetallocene catalyst compounds are those where the R* substituents onthe bulky ligands L^(A) and L^(B) of Formulas 1 and 2 are substitutedwith the same or different number of substituents on each of the bulkyligands. In another embodiment, the bulky ligands L^(A) and L^(B) ofFormulas 1 and 2 are different from each other.

Other bulky ligand metallocene catalyst compounds and catalyst systemsuseful in the invention may include those described in U.S. Patent Nos.5,064,802, 5,145,819, 5,149,819, 5,243,001, 5,239,022, 5,276,208,5,296,434, 5,321,106, 5,329,031, 5,304,614, 5,677,401, 5,723,398,5,753,578, 5,854,363, 5,856,547 5,858,903, 5,859,158, 5,900,517 and5,939,503 and PCT publications WO 93/08221, WO 93/08199, WO 95/07140, WO98/11144, WO 98/41530, WO 98/41529, WO 98/46650, WO 99/02540 and WO99/14221 and European publications EP-A-0 578 838, EP-A-0 638 595,EP-B-0 513 380, EP-A1-0 816 372, EP-A2-0 839 834, EP-B1-0 632 819,EP-B1-0 748 821 and EP-B1-0 757 996, all of which are herein fullyincorporated by reference.

In another embodiment, the catalyst compositions useful in the inventionmay include bridged heteroatom, mono-bulky ligand metallocene compounds.These types of catalysts and catalyst systems are described in, forexample, PCT publication WO 92/00333, WO 94/07928, WO 91/04257, WO94/03506, W096/00244, WO 97/15602 and WO 99/20637 and U.S. Pat. Nos.5,057,475, 5,096,867, 5,055,438, 5,198,401, 5,227,440 and 5,264,405 andEuropean publication EP-A-0 420 436, all of which are herein fullyincorporated by reference.

In another embodiment, the catalyst composition useful in the inventionincludes one or more bulky ligand metallocene catalyst compoundsrepresented by Formula 3:L^(C)A*J*MQ*_(n)  (3)where M is a Group 3 to 16 metal atom or a metal selected from the Groupof actinides and lanthanides of the Periodic Table of Elements,preferably M is a Group 3 to 12 transition metal, and more preferably Mis a Group 4, 5 or 6 transition metal, and most preferably M is a Group4 transition metal in any oxidation state, and is especially titanium;L^(C) is a substituted or unsubstituted bulky ligand bonded to M; J* isbonded to M; A* is bonded to J* and L^(C); J* is a heteroatom ancillaryligand; and A* is a bridging group; Q* is a univalent anionic ligand;and n is the integer 0, 1 or 2. In Formula 3 above, L^(C), A* and J*form a fused ring system. In an embodiment. L^(C) of Formula 3 is asdefined above for L^(A). A*, M and Q* of Formula 3 are as defined abovein Formula 1. In Formula 3, J* is a heteroatom containing ligand inwhich J* is an element with a coordination number of three from Group 15or an element with a coordination number of two from Group 16 of thePeriodic Table of Elements. Preferably J* contains a nitrogen,phosphorus, oxygen or sulfur atom with nitrogen being most preferred. Inan embodiment of the invention, the bulky ligand metallocene catalystcompounds are heterocyclic ligand complexes where the bulky ligands, thering(s) or ring system(s), include one or more heteroatoms or acombination thereof. Non-limiting examples of heteroatoms include aGroup 13 to 16 element, preferably nitrogen, boron, sulfur, oxygen,aluminum, silicon, phosphorous and tin. Examples of these bulky ligandmetallocene catalyst compounds are described in WO 96/33202, WO96/34021, WO 97/17379 and WO 98/22486 and EP-A1-0 874 005 and U.S. Pat.No. 5,637,660, 5,539,124, 5,554,775, 5,756,611, 5,233,049, 5,744,417,and 5,856,258 all of which are herein incorporated by reference.

In one embodiment, the bulky ligand metallocene compounds(pre-catalysts) are those complexes based on bidentate ligandscontaining pyridine or quinoline moieties, such as those described inU.S. application Ser. No. 09/103,620 filed June 23, 1998, which isherein incorporated by reference. In another embodiment, the bulkyligand metallocene catalyst compounds are those described in PCTpublications WO 99/01481 and WO 98/42664, which are fully incorporatedherein by reference.

In another embodiment, the bulky ligand metallocene catalyst compound isa complex of a metal, preferably a transition metal, a bulky ligand,preferably a substituted or unsubstituted pi-bonded ligand, and one ormore heteroallyl moieties, such as those described in U.S. Pat. Nos.5,527,752 and 5,747,406 and EP-B1-0 735 057, all of which are hereinfully incorporated by reference.

In another embodiment, the bulky ligand metallocene catalyst compoundsare those described in PCT publications WO 99/01481 and WO 98/42664,which are fully incorporated herein by reference.

Useful Group 6 bulky ligand metallocene catalyst systems are describedin U.S. Pat. No. 5,942,462, which is incorporated herein by reference.

Still other useful catalysts include those multinuclear metallocenecatalysts as described in WO 99/20665 and U.S. Pat. No. 6,010,794, andtransition metal metaaracyle structures described in EP 0 969 101 A2,which are herein incorporated herein by reference. Other metallocenecatalysts include those described in EP 0 950 667 A1, doublecross-linked metallocene catalysts (EP 0 970 074 A1), tetheredmetallocenes (EP 970 963 A2) and those sulfonyl catalysts described inU.S. Pat. No. 6,008,394, which are incorporated herein by reference.

It is also contemplated that in one embodiment the bulky ligandmetallocene catalysts, described above, include their structural oroptical or enantiomeric isomers (meso and racemic isomers, for examplesee U.S. Pat. No. 5,852,143, incorporated herein by reference) andmixtures thereof.

It is further contemplated that any one of the bulky ligand metallocenecatalyst compounds, described above, have at least one fluoride orfluorine containing leaving group as described in U.S. application Ser.No. 09/191,916 filed Nov. 13, 1998.

The Group 15 containing metal compounds utilized in the catalystcomposition of the invention are prepared by methods known in the art,such as those disclosed in EP 0 893 454 A1, U.S. Pat. No. 5,889,128 andthe references cited in U.S. Pat. No. 5,889,128 which are all hereinincorporated by reference. U.S. application Ser. No. 09/312,878, filedMay 17, 1999, discloses a gas or slurry phase polymerization processusing a supported bisamide catalyst, which is also incorporated hereinby reference.

For additional information of Group 15 containing metal compounds,please see Mitsui Chemicals, Inc. in EP 0 893 454 A1 which disclosestransition metal amides combined with activators to polymerize olefins.

In one embodiment the Group 15 containing metal compound is allowed toage prior to use as a polymerization. It has been noted on at least oneoccasion that one such catalyst compound (aged at least 48 hours)performed better than a newly prepared catalyst compound.

It is further contemplated that bis-amide based pre-catalysts may beused. Exemplary compounds include those described in the patentliterature. International patent publications WO 96/23010, WO 97/48735and Gibson, et al., Chem. Comm., pp. 849-850 (1998), which disclosediimine-based ligands for Group-8-10 compounds that undergo ionicactivation and polymerize olefins. Polymerization catalyst systems fromGroup-5-10 metals, in which the active center is highly oxidized andstabilized by low-coordination-number, polyanionic, ligand systems, aredescribed in U.S. Pat. No. 5,502,124 and its divisional U.S. Pat. No.5,504,049. See also the Group-5 organometallic catalyst compounds ofU.S. Pat. No. 5,851,945 and the tridentate-ligand-containing,Group-5-10, organometallic catalysts of U.S. Pat. No. 6, 294, 495.Group-11 catalyst precursor compounds, activatable with ionizingcocatalysts, useful for olefin and vinylic polar molecules are describedin WO 99/30822.

Other useful catalyst compounds are those Group 5 and 6 metal imidocomplexes described in EP-A2-0 816 384 and U.S. Pat. No. 5,851,945,which is incorporated herein by reference. In addition, metallocenecatalysts include bridged bis(arylamido) Group 4 compounds described byD. H. McConville, et al., in Organometallics 1995, 14, 5478-5480, whichis herein incorporated by reference. In addition, bridged bis(amido)catalyst compounds are described in WO 96/27439, which is hereinincorporated by reference. Other useful catalysts are described asbis(hydroxy aromatic nitrogen ligands) in U.S. Pat. No. 5,852,146, whichis incorporated herein by reference. Other useful catalysts containingone or more Group 15 atoms include those described in WO 98/46651, whichis herein incorporated herein by reference.

U.S. Pat. No. 5,318,935 describes bridged and unbridged, bisamidocatalyst compounds of Group-4 metals capable of alpha-olefinspolymerization. Bridged bi(arylamido)-Group-4 compounds for olefinpolymerization are described by D. H. McConville, et al. inOrganometallics 1995, 14, 5478-5480. This reference presents syntheticmethods and compound characterizations. Further work appearing in D. H.McConville, et al, Macromolecules 1996, 29, 5241-5243, describes bridgedbis(arylamido)-Group-4 compounds that are polymerization catalysts for1-hexene. Additional invention-suitable transition metal compoundsinclude those described in WO 96/40805. Cationic Group-3- orLanthanide-metal olefin polymerization complexes are disclosed incopending U.S. application Ser. No. 09/408,050, filed 29 Sep. 1999. Amonoanionic bidentate ligand and two monoanioiiic ligands stabilizethose catalyst precursors, which can be activated with this invention'sionic cocatalysts.

The literature describes many additional suitable catalyst-precursorcompounds. Compounds that contain abstractable ligands or that can bealkylated to contain abstractable ligands suit this invention. See, forinstance, V. C. Gibson, et al; “The Search for New-Generation OlefinPolymerization Catalysts: Life Beyond Metallocenes”, Angew. Chef. Int.Ed., 38, 428-447 (1999).

This invention may also be practiced with the catalysts containingphenoxide ligands such as those disclosed in EP 0 874 005 A1, which inincorporated by reference herein.

In another embodiment, conventional-type transition metal catalysts maybe used in the practice of this invention. Conventional-type transitionmetal catalysts are those traditional Ziegler-Natta, vanadium andPhillips-type catalysts well known in the art. Such as, for exampleZiegler-Natta catalysts as described in Ziegler-Natta Catalysts andPolymerizations, John Boor, Academic Press, New York, 1979. Examples ofconventional-type transition metal catalysts are also discussed in U.S.Pat. Nos. 4,115,639, 4,077,904, 4,482,687, 4,564,605, 4,721,763,4,879,359 and 4,960,741, all of which are herein fully incorporated byreference. The conventional-type transition metal catalyst compoundsthat may be used in the present invention include transition metalcompounds from Groups 3 to 17, preferably 4 to 12, more preferably 4 to6 of the Periodic Table of Elements.

Preferred conventional-type transition metal catalysts may berepresented by the formula: MR_(x), where M is a metal from Groups 3 to17, preferably Group 4 to 6, more preferably Group 4, most preferablytitanium; R is a halogen or a hydrocarbyloxy group; and x is theoxidation state of the metal M. Non-limiting examples of R includealkoxy, phenoxy, bromide, chloride and fluoride. Non-limiting examplesof (conventional-type transition metal catalysts where M is titaniuminclude TiCl₄, TiBr₄, Ti(OC₂H₅)₃Cl, Ti(OC₂H₅)Cl₃, Ti(OC₄H₉)₃Cl,Ti(OC₃H₇)₂Cl₂, Ti(OC₂H₅)₂Br₂, TiCl₃.1/3AlCl₃ and Ti(OCl₁₂H₂₅)Cl₃.

Conventional-type transition metal catalyst compounds based onmagnesium/titanium electron-donor complexes that are useful in theinvention are described in, for example, U.S. Pat. Nos. 4,302,565 and4,302,566, which are herein fully incorporate by reference. The MgTiCl₆(ethyl acetate)₄ derivative is particularly preferred.

British Patent Application 2,105,355 and U.S. Pat. No. 5,317,036, hereinincorporated by reference, describes various conventional-type vanadiumcatalyst compounds. Non-limiting examples of conventional-type vanadiumcatalyst compounds include vanadyl trihalide, alkoxy halides andalkoxides such as VOCl₃, VOCl₂(OBu) where Bu=butyl and VO(OC₂H₅)₃;vanadium tetra-halide and vanadium alkoxy halides such as VCl₄ andVCl₃(OBu); vanadium and vanadyl acetyl acetonates and chloroacetylacetonates such as V(AcAc)₃ and VOCl₂(AcAc) where (AcAc) is an acetylacetonate. The preferred conventional-type vanadium catalyst compoundsare VOCl₃, VCl₄ and VOCl₂—OR where R is a hydrocarbon radical,preferably a C₁ to C₁₀ aliphatic or aromatic hydrocarbon radical such asethyl, phenyl, isopropyl, butyl, propyl, n-butyl, iso-butyl,tertiary-butyl, hexyl, cyclohexyl, naphthyl, etc., and vanadium acetylacetonates.

Conventional-type chromium catalyst compounds, often referred to asPhillips-type catalysts, suitable for use in the present inventioninclude CrO₃, chromocene, silyl chromate, chromyl chloride (CrO₂Cl₂),chromium-2-ethyl-hexanoate, chromium acetylacetonate (Cr(AcAc)₃), andthe like. Non-limiting examples are disclosed in U.S. Pat. Nos.3,709,853, 3,709,954, 3,231,550, 3,242,099 and 4,077,904, which areherein fully incorporated by reference.

Still other conventional-type transition metal catalyst compounds andcatalyst systems suitable for use in the present invention are disclosedin U.S. Pat. Nos. 4,124,532, 4,302,565, 4,302,566, 4,376,062, 4,379,758,5,066,737, 5,763,723, 5,849,655, 5,852,144, 5,854,164 and 5,869,585 andpublished EP-A2 0 416 815 A2 and EP-A1 0 420 436, which are all hereinincorporated by reference.

Other catalysts may include cationic catalysts such as AlCl₃, and othercobalt, iron, nickel and palladium catalysts well known in the art. Seefor example U.S. Pat. Nos. 3,487,112, 4,472,559, 4,182,814 and4,689,437, all of which are incorporated herein by reference.

It is also contemplated that other catalysts can be combined with thecatalyst compounds in the catalysts composition useful in the invention.For example, see U.S. Pat. Nos. 4,937,299, 4,935,474, 5,281,679,5,359,015, 5,470,811, and 5,719,241 all of which are herein fullyincorporated herein reference.

It is further contemplated that one or more of the catalyst compoundsdescribed above or catalyst systems may be used in combination with oneor more conventional catalyst compounds or catalyst systems.Non-limiting examples of mixed catalysts and catalyst systems aredescribed in U.S. Pat. Nos. 4,159,965, 4,325,837, 4,701,432, 5,124,418,5,077,255, 5,183,867, 5,391,660, 5,395,810, 5,691,264, 5,723,399 and5,767,031 and PCT Publication WO 96/23010 published Aug. 1, 1996, all ofwhich are herein fully incorporated by reference.

Preferred metallocene catalysts used in this invention can morespecifically be represented by one of the following general formulae(all references to Groups being the new Group notation of the PeriodTable of the Elements as described by Chemical and Engineering News,63(5), 27, 1985):

wherein:

-   (A-Cp) is either (Cp), (Cp*) or Cp-A′-Cp*; Cp and Cp* are the same    or different cyclopentadienyl rings substituted with from zero to    five substituent groups S″, each substituent group S″ being,    independently, a radical group which is a hydrocarbyl,    substituted-hydrocarbyl, halocarbyl, substituted-halocarbyl,    hydrocarbyl-substituted organometalloid, halocarbyl-substituted    organometalloid, disubstituted boron, disubstituted pnictogen,    substituted chalcogen or halogen radicals, or Cp and Cp* are    cyclopentadienyl rings in which any two adjacent S″ groups are    joined forming a C₄ to C₂₀ ring to give a saturated or unsaturated    polycyclic cyclopentadienyl ligand; Cp and Cp* may also have one or    two carbon atoms within the ring replaced by a Group 15 or 16    element especially, S, O, N or P;-   A′ is a bridging group;-   (C₅H_(5-y -x)S″_(x)) is a cyclopentadienyl ring substituted with    from zero to five S″ radicals as defined above;-   x is from 0 to 5 denoting the degree of substitution;-   M is titanium, zirconium or hafnium;-   X₁ is a hydride radical, hydrocarbyl radical, substituted-    hydrocarbyl radical, hydrocarbyl-substituted organometalloid radical    or halocarbyl-substituted organometalloid radical which radical may    optionally be covalently bonded to both or either M and L or L′ or    all or any M, S″ or S′, and provided that X₁ is not a substituted or    unsubstituted cyclopentadienyl ring;-   (JS′_(z-1-y)) is a heteroatom ligand in which J is an element from    Group 15 of the Periodic Table of Elements with a coordination    number of 3 or an element from Group 16 with a coordination number    of 2; S′ is a radical group which is a hydrocarbyl, substituted    hydrocarbyl, halocarbyl, substituted halocarbyl,    hydrocarbyl-substituted organometalloid, or halocarbyl-substituted    organometalloid; and z is the coordination number of the element J;-   y is 0 or 1;-   L is an olefin, diolefin or aryne ligand L′ is the same as L, and    can additionally be an amine, phosphine, ether, or sulfide ligand,    or any other neutral Lewis base; L′ can also be a second transition    metal compound of the same type such that the two metal center M and    M* are bridged by X₁ and X′₁, wherein M* has the same meaning as M,    X′₁, X₂ and X′₂ have the same meaning as X₁, where such dimeric    compounds which are precursors to the, cationic portion of the    catalyst are represented by the formula:    wherein-   w is an integer from 0 to 3;-   B′ is a chemically stable, non-nucleophilic anionic complex having a    molecular diameter about or greater than 4 Angstroms or an anionic    Lewis-acid activator resulting from the reaction of a Lewis-acid    activator with the precursor to the cationic portion of the catalyst    system described in formulae 1-4. When B′ is a Lewis-acid activator,    X₁ can also be an alkyl group donated by the Lewis-acid activator;    and-   d is an integer representing the charge of B′.

The catalysts are preferably prepared by combining at least twocomponents. In one preferred method, the first component is acyclopentadienyl derivative of a Group 4 metal compound containing atleast one ligand which will combine with the second component or atleast a portion thereof such as a cation portion thereof. The secondcomponent is an ion-exchange compound comprising a cation which willirreversibly react with at least one ligand contained in said Group 4metal compound (first component) and a non-coordinating anion which iseither a single coordination complex comprising a plurality oflipophilic radicals covalently coordinated to and shielding a centralformally charge-bearing metal or metalloid atom or an anion comprising aplurality of boron atoms such as polyhedral boranes, carboranes andmetallacarboranes.

In general, suitable anions for the second component may be any stableand bulky anionic complex having the following molecular attributes: 1)the anion should have a molecular diameter greater than 4 Angstroms; 2)the anion should form stable ammonium salts; 3) the negative charge onthe anion should be delocalized over the framework of the anion or belocalized within the core of the anion; 4) the anion should be arelatively poor nucleophile; and 5) the anion should not be a powerfulreducing or oxidizing agent. Anions meeting these criteria—such aspolynuclear boranes, carboranes, metallacarboranes, polyoxoanions andanionic coordination complexes are well described in the chemicalliterature.

The cation portion of the second component may comprise Bronsted acidssuch as protons or protonated Lewis bases or may comprise Lewis acidssuch as ferricinum, tropylium, triphenylcarbenium or silver cations.

In another preferred method, the second component is a Lewis-acidcomplex which will react with at least one ligand of the firstcomponent, thereby forming an ionic species described in formulae 4-6with the ligand abstracted from the first component now bound to thesecond component. Alumoxanes and especially methylalumoxane, the productformed from the reaction of trimethylaluminum in an aliphatic oraromatic hydrocarbon with stoichiometric quantities of water, areparticularly preferred Lewis-acid second components. Modified alumoxanesare also preferred. Alumoxanes are well known in the art and methods fortheir preparation are :illustrated by U.S. Pat. Nos. 4,542,199;4,544,762; 5, 015,749; and 5,041,585. A technique for preparing modifiedalumoxanes has been disclosed in U.S. Pat. No. 5,041,584, in EPA 0 516476, and in EPA 0 561 476, which are incorporated by reference herein.

Upon combination of the first and second components, the secondcomponent reacts with one of the ligands of the first component, therebygenerating an anion pair consisting of a Group 4 metal cation and theaforementioned anion, which anion is compatible with and non-coordinating towards the Group 4 metal cation formed from the firstcomponent. The anion of the second compound must be capable ofstabilizing the Group 4 metal cation's ability to function as a catalystand must be sufficiently labile to permit displacement by an olefin,diolefin or an acetylenically unsaturated monomer during polymerization.The catalysts of this invention may be supported. U.S. Pat. No.4,808,561, issued Feb. 28, 1989; U.S. Pat. No. 4,897,455 issued Jan. 3,1990; U.S. Pat. No. 5,057,475 issued Oct. 15, 1991; U.S. patentapplication Ser. No. 459,921 (published as PCT International publicationWO 91/09882), Canadian Patent 1,268,753, U.S. Pat. No. 5,240,894 and WO94 03506 disclose such supported catalysts and the methods to producesuch and are herein incorporated by reference.

The Group 4 metal compounds; i.e., titanium, zirconium and hafniummetallocene compounds, useful as first compounds (pre-catalysts) in thepreparation of the preferred metallocene catalysts of this invention arecyclopentadienyl derivatives of titanium, zirconium and hafnium. Ingeneral, useful titanocenes, zirconocenes and hafnocenes may berepresented by the following general formulae:

wherein:

-   (A-Cp) is either (Cp)(Cp*) or Cp-A′-Cp*; Cp and Cp* are the same or    different cyclopentadienyl rings substituted with from zero to five    substituent groups S″, each substituent group S″ being,    independently, a radical group which is a hydrocarbyl,    substituted-hydrocarbyl, halocarbyl, substituted-halocarbyl,    hydrocarbyl-substituted organometalloid, halocarbyl-substituted    organometalloid, disubstituted boron, disubstituted pnictogen,    substituted chalcogen or halogen radicals, or Cp and Cp* are    cyclopentadienyl rings in which any two adjacent S″ groups are    joined forming a C₄ to C₂₀ ring to give a saturated or unsaturated    polycyclic cyclopentadienyl ligand;-   A′ is a bridging group;-   y is 0 or 1;-   (C₅H_(5-y-x)S″_(x)) is a cyclopentadienyl ring substituted with from    zero to five S″ radicals as defined above;-   x is from 0 to 5 denoting the degree of substitution;-   (JS′_(z-1-y)) is a heteroatom ligand in which J is an element from    Group 15 of the Periodic Table of Elements with a coordination    number of 3 or an element from Group 16 with a coordination number    of 2, S′ is a radical group which is a hydrocarbyl, substituted    hydrocarbyl, halocarbyl, substituted halocarbyl,    hydrocarbyl-substituted organometalloid, or halocarbyl-substituted    organometalloid; and z is the coordination number of the element J;-   L is an olefin, diolefin or aryne ligand. L′ is the same as L and    can additionally be an amine, phosphine, ether, or sulfide ligand,    or any other neutral Lewis base; L′ can also be a second transition    metal compound of the same type such that the two metal centers M    and M* are bridged by X₁ and X′₁, wherein M* has the same meaning as    M, X′₁ has the same meaning as X₁ and X′₂ has the same meaning as X₂    where such dimeric compounds which are precursors to the cationic    portion of the catalyst are represented by formula 7 above;-   w is an integer from 0 to 3; and-   X₁ and X₂ are, independently, hydride radicals, hydrocarbyl    radicals, substituted hydrocarbyl radicals, halocarbyl radicals,    substituted halocarbyl radicals, and hydrocarbyl- and    halocarbyl-substituted organometalloid radicals, substituted    pnictogen radicals, or substituted chalcogen radicals; or X₁ and X₂    are joined and bound to the metal atom to form a metallacycle ring    containing from about 3 to about 20 carbon atoms; or X₁ and X₂    together can be an olefin, diolefin or aryne ligand; or when    Lewis-acid activator,, such as methylalumoxane, which are capable of    donating an X₁ ligand as described above to the transition metal    component are used, X₁ and X₂ may independently be a halogen,    alkoxide, aryloxide, amide, phosphide or other univalent anionic    ligand or both X₁ and X₂ can also be joined to form a anionic    chelating ligand and with the proviso that X₁ and X₂ are not a    substituted or unsubstituted cyclopentadienyl ring.

Table A depicts representative constituent moieties for the metallocenecomponents of formulae 7-10. The list is for illustrative purposes onlyand should not be construed to be limiting in any way. A number of finalcomponents may be formed by permuting all possible combinations of theconstituent moieties with each other. When hydrocarbyl radicalsincluding alkyl, alkenyl, alkynyl, cycloalkyl, cycloalkenyl,cycloalkynyl and aromatic radicals are disclosed in this application theterm includes all isomers. For example, butyl includes n-butyl,2-methylpropyl, 1-methylpropyl, tert-butyl, and cyclobutyl; pentylincludes n-pentyl, 1-methylbutyl, 2-methylbutyl, 3-methylbutyl,1-ethylpropyl, neopentyl, cyclopentyl and methylcyclobutyl; butenylincludes E and Z forms of 1-butenyl, 2-butenyl, 3-butenyl,1-methyl-1-propenyl, 1-methyl-2-propenyl, 2-methyl-1-propenyl and2-methyl-2-propenyl. This includes when a radical is bonded to anothergroup, for example, propylcyclopentadienyl includen-propylcyclopentadienyl, isopropylcyclcopentadienyl andcyclopropylcyclopentadienyl. In general, the ligands or groupsillustrated in Table A include all isomeric forms. For example,dimethylcyclopentadienyl includes 1,2-dimethylcyclopentadienyl and1,3-dimethylcyclopentadienyl; methylindenyl includes 1-methylindenyl,2-methylindenyl, 3-methylindenyl, 4-methylindenyl, 5-methylindenyl,6-methylindenyl and 7-methylindenyl; methylethylphenyl includesortho-methylethylphenyl, meta-methylethylphenyl andpara-methylethylphenyl. Examples of specific invention catalystprecursors take the following formula where some components are listedin Table A. To illustrate members of the transition metal component,select any combination of the species listed in Tables A. Fornomenclature purposes, for the bridging group, A′, the words “silyl” and“silylene” are used interchangeably, and represent a diradical species.For the bridging group A′, “ethylene” refers to a 1,2-ethylene linkageand is distinguished from ethene-1,1-diyl. Thus, for the bridging groupA′, “ethylene” and “1,2-ethylene” are used interchangeably. Forcompounds processing a bridging group, A′, the bridge position on thecyclopentadienyl-type ring is always considered the 1-position. Thus,for example, the use of “1-fluorenyl” is interchangeable with the use of“fluorenyl”

Illustrative compounds of the formula 8 type are:bis(cyclopentadienyl)hafnium dimethyl,ethylenebis(tetrahydroindenyl)zirconium dihidryde,bis(pentamethyl)zirconium diethyl,dimethylsilyl(1-fluorenyl)(cyclopentadienyl)titanium dichloride and thelike. Illustrative compounds of the formula 9 type are:bis(cyclopentadienyl)(1,3-butadiene)zirconium,bis(cyclopentadienyl)(2,3-dimethyl-1,3-butadiene)zirconium,bis(pentamethylcyclopentadienyl)(benzene)zirconium,bis(pentamethylcyclopentadienyl)titanium ethylene and the like.Illustrative compounds of the formula 10 type are:dimethylsilyl(tetramethylcyclopentadienyl)(t-butylamido)zirconiumdichloride, ethylene(methylcyclopentadienyl)(phenylamido)titaniumdimethyl, methylphenylsilyl(indenyl)(phenyphosphido)hafnium dihydrideand (pentamethylcyclopentadienyl)(di-t-butylamido)hafnium dimethoxide.

The conditions under which complexes containing neutral Lewis baseligands such as ether or those which form dimeric compounds isdetermined by the steric bulk of the ligands about the metal center. Forexample, the t-butyl group in Me₂Si(Me₄C₅)(N-t-Bu)ZrCl₂ has greatersteric requirements that the phenyl in Me₂Si(Me₄C₅)(NPh)ZrCl₂.Et₂Othereby not permitting ether coordination in the former compound in itssolid state. Similarly, due to the decreased steric bulk of thetrimethylsilylcyclopentadienyl group in [Me₂Si(Me₃SiC₅H₃)(N-t-Bu)ZrCl₂]₂versus that of the tetramethylcyclopentadienyl group inMe₂Si(Me₄C₅)(N-t-Bu)ZrCl₂, the former compound is dimeric and the latteris not. TABLE A A′ Dimethylsilylene Diethylsilylene dipropylsilylenedibutylsilylene dipentylsilylene dihexylsilylene diheptylsilylenedioctylsilylene dinonylsilylene didecylsilylene diundecylsilylenedidodecylsilylene ditridecylsilylene ditetradecylsilylenedipentadecylsilylene dihexadecylsilylene diheptadecylsilylenedioctadecylsilylene dinonadecylsilylene dieicosylsilylenediheneicosylsilylene didocosylsilylene ditricosylsilyleneditetracosylsilylene dipentacosylsilylene dihexacosylsilylenediheptacosylsilylene dioctacosylsilylene dinonacosylsilyleneditriacontylsilylene dicyclohexylsilylene dicyclopentylsilylenedicycloheptylsilylene dicyclooctylsilylene dicyclodecylsilylenedicyclododecylsilylene dinapthylsilylene diphenylsilyleneditolylsilylene dibenzylsilylene diphenethylsilylenedi(butylphenethyl)silylene methylethylsilylene methylpropylsilylenemethylbutylsilylene methylhexylsilylene methylphenylsilyleneethylphenylsilylene ethylpropylsilylene ethylbutylsilylenepropylphenylsilylene dimethylgermylene diethylgermylenediphenylgermylene methylphenylgermylene CyclotetramethylenesilylenCyclopentamethylenesilyle cyclotrimethylenesilylene cyclohexylazanediylbutylazanediyl methylazanediyl phenylazanediyl perfluorophenylazanediylmethylphosphanediyl ethylphosphanediyl propylphosphanediylbutylphosphanediyl cyclohexylphosphanediyl phenylphosphanediylmethylboranediyl phenylboranediyl methylene dimethylmethylenediethylmethylene dibutylmethylene dipropylmethylene diphenylmethyleneditolylmethylene di(butylphenyl)methylene di(trimethylsilylphenyl)metdi(triethylsilylphenyl)methy dibenzylmethylene CyclotetramethylenemethylCyclopentamethylenemethy ethylene methylethylene dimethylethylenetrimethylethylene tetramethylethylene cyclopentylene cyclohexylenecycloheptylene cyclooctylene propanediyl methylpropanediyldimethylpropanediyl trimethylpropanediyl tetramethylpropanediylpentamethylpropanediyl hexamethylpropanediyl tetramethyldisiloxylenevinylene ethene-1,1-diyl divinylsilylene dipropenylsilylenedibutenylsilylene methylvinylsilylene methylpropenylsilylenemethylbutenylsilylene dimethylsilylmethylene diphenylsilylmethylenedimethylsilylethylene diphenylsilylethylene dimethylsilylpropylenediphenylsilylpropylene dimethylstannylene diphenylstannylene Cp, Cp*,CpR or (C₅H_(5-y-x)S″_(x)) Cyclopentadienyl MethylcyclopentadienylDimethylcyclopentadienyl TrimethylcyclopentadienylTetramethylcyclopentadienyl Pentamethylcyclopentadienyl (no A′)Ethylcyclopentadienyl Diethylcyclopentadienyl PropylcyclopentadienylDipropylcyclopentadienyl Butylcyclopentadienyl DibutylcyclopentadienylPentylcyclopentadienyl Dipentylcyclopentadienyl HexylcyclopentadienylDihexylcyclopentadienyl Heptylcyclopentadienyl Diheptylcyclopentadienyloctylcyclopentadienyl dioctylcyclopentadienyl nonylcyclopentadienyldinonylcyclopentadienyl decylcyclopentadienyl didecylcyclopentadienylundecylcyclopentadienyl dodecylcyclopentadienyl tridecylcyclopentadienyltetradecylcyclopentadienyl pentadecylcyclopentadienyl (no A′)hexadecylcyclopentadienyl heptadecylcyclopentadienyloctadecylcyclopentadienyl nonadecylcyclopentadienyleicosylcyclopentadienyl heneicosylcyclopentadienyldocosylcyclopentadienyl tricosylcyclopentadienyltetracosylcyclopentadienyl pentacosylcyclopentadienylhexacosylcyclopentadienyl heptacosylcyclopentadienyloctacosylcyclopentadienyl nonacosylcyclopentadienyltriacontylcyclopentadienyl cyclohexylcyclopentadienylphenylcyclopentadienyl diphenylcyclopentadienyltriphenylcyclopentadienyl tetraphenylcyclopentadienylpentaphenylcyclopentadienyl tolylcyclopentadineyl benzylcyclopentadienylphenethylcyclopentadienyl cyclohexylmethylcyclopentadienylnapthylcyclopentadienyl methylphenylcyclopentadienylmethyltolylcyclopentadienyl methylethylcyclopentadienylmethylpropylcyclopentadienyl methylbutylcyclopentadienylmethylpentylcyclopentadienyl methylhexylcyclopentadienylmethylheptylcyclpentadienyl methyloctylcyclopentadienylmethylnonylcyclopentadienyl methyldecylcyclopentadienylvinylcyclopentadienyl propenylcyclopentadienyl butenylcyclopentadienylindenyl methylindenyl dimethylindenyl trimethylindenylmethylpropylindenyl dimethylpropylindenyl methyldipropylindenylmethylethylindenyl methylbutylindenyl ethylindenyl propylindenylbutylindenyl pentylindenyl hexylindenyl heptylindenyl octylindenylnonylindenyl decylindenyl phenylindenyl (fluorophenyl)indenyl(methylphenyl)indenyl biphenylindenyl(bis(trifluoromethyl)phenyl)indenyl napthylindenyl phenanthrylindenylbenzylindenyl benzindenyl cyclohexylindenyl methylphenylindenylethylphenylindenyl propylphenylindenyl methylnapthylindenylethylnapthylindenyl propylnapthylindenyl (methylphenyl)indenyl(dimethylphenyl)indenyl (ethylphenyl)indenyl (diethylphenyl)indenyl(propylphenyl)indenyl (dipropylphenyl)indenyl methyltetrahydroindenyldimethyltetrahydroindenyl dimethyldihydroindenyl dimethyltrihydroindenylmethylphenyltetrahydroindenyl methylphenyldihydroindenylmethylphenyltrihydroindenyl ethyltetrahydroindenylpropyltetrahydroindenyl butyltetrahydroindenyl phenyltetrahydroindenylfluorenyl methylfluorenyl dimethylfluorenyl trimethylfluorenylethylfluorenyl propylfluorenyl butylfluorenyl dibutylfluorenylpentylfluorenyl hexylfluorenyl heptylfluorenyl octylfluorenylnonylfluorenyl decylfluorenyl phenylfluorenyl napthylfluorenylbenzylfluorenyl methylphenylfluorenyl ethylphenylfluorenylpropylphenylfluorenyl methylnapthylfluorenyl ethylnapthylfluorenylpropylnapthylfluorenyl octahydrofluorenyl tetrahydrofluorenyloctamethyloctahydrodibenzo[b,h]fluorenyltetramethyltetrahydrobenzo[b]fluorenyl diphenylmethylcyclopentadienyltrimethylsilylcyclopentadienyl triethylsilylcyclopentadienyltrimethylgermylcyclopentadienyl trimethylstannylcyclopentadienyltriethylplumbylcyclopentadienyl trifluromethylcyclopentadienylN,N-dimethylamidocyclopentadienyl P,P-dimethylphosphidocyclopentadienylN,N-diethylamidocyclopentadienyl methoxycyclopentadienylethoxycyclopentadienyl trimethylsiloxycyclopentadienyl(N,N-dimethylamidomethyl)cyclopentadienyl methyoxyindenyldimethyoxyindenyl N,N-dimethylaminoindenyl trimethylsiloxyindenylbutyldimethylsiloxyindenyl bis(N,N-dimethylamino)indenyldi(trimethylsiloxy)indenyl di(butyldimethylsiloxy)indenylmethoxyfluorenyl dimethoxyfluorenyl N,N-dimethylaminofluorenyltrimethylsiloxyfluorenyl butyldimethylsiloxyfluorenyl dimethoxyfluorenylbis(N,N-dimethylamino)fluorenyl di(trimethylsiloxy)fluorenyldi(butyldimethylsiloxy)fluorenyl (JS′_(z−1−y)) (y = 1) methylamidoethylamido propylamido butylamido pentylamido hexylamido heptylamidooctylamido nonylamido decylamido eicosylamido heneicosylamidodocosylamido tricosylamido tetracosylamido pentacosylamidohexacosylamido heptacosylamido octacosylamido nonacosylamidotriacontylamido phenylamido tolylamido phenethylamido benzylamidocyclobutylamido cyclopentylamido cyclohexylamido cycloheptylamidocyclooctylamido cyclononylamido cyclodecylamido cyclododecylamidoadamantylamido norbornylamido perfluorophenylamido fluorophenylamidodifluorophenylamido oxo sulfido (JS′_(z−1−y)) (y = 0) methoxide ethoxidephenoxide dimethylphenoxide dipropylphenoxide methylthio ethylthiophenylthio dimethylphenylthio dipropylphenylthio X₁ or X₂ chloridebromide iodide fluoride hydride methyl ethyl propyl butyl pentyl hexylheptyl octyl nonyl decyl undecyl dodecyl tridecyl tetradecyl pentadecylhexadecyl heptadecyl octadecyl nonadecyl eicosyl heneicosyl docosyltricosyl tetracosyl pentacosyl hexacosyl heptacosyl octacosyl nonacosyltriacontyl phenyl benzyl phenethyl tolyl methoxy ethoxy propoxy butoxydimethylamido diethylamido methylethylamido phenoxy benzoxy allyl X₁ andX₂ together methylidene ethylidene propylidene tetramethylenepentamethylene hexamethylene ethylenedihydroxy butadiene methylbutadienedimethylbutadiene pentadiene methylpentadiene dimethylpentadienehexadiene methylhexadiene dimethylhexadiene M titanium zirconium hafniumL or L′ (optional) ethylene propylene butene hexene styrene hexadienebutadiene dimethylbutadiene pentadiene methylhexadiene dimethylhexadieneacetylene methylacetylene ethylacetylene benzyne cyclopentenecyclohexene L′ (optional) diethylether dimethylether trimethylaminetriphenylamine triethylamine tricyclohexylphosphine triphenylphosphinetrimethylphosphine tetrahydrofuran furan thiophene dimethylsulfidediphenylsulfide

Additional preferred catalysts include those described in WO 01/48034,which is incorporated herein by reference. Particularly preferredcatalyst compounds include those disclosed at page 9, line 38 to page25, line 42, page 28, lines 5 to 17, and page 30, line 37 to page 35,line 28.

Activators and Activation Methods for Catalyst Compounds

The polymerization pre-catalyst compounds, described above, aretypically activated in various ways to yield compounds having a vacantcoordination site that will coordinate, insert, and polymerizeolefin(s). For the purposes of this patent specification and appendedclaims, the terms “cocatalyst” and “activator” are used hereininterchangeably and are defined to be any compound which can activateany one of the catalyst compounds described above by converting theneutral catalyst compound to a catalytically active catalyst compoundcation. Non-limiting activators, for example, include alumoxanes,aluminum alkyls, ionizing activators, which may be neutral or ionic, andconventional-type cocatalysts. Preferred activators typically includealumoxane compounds, modified alumoxane compounds, and ionizing anionprecursor compounds that abstract one reactive., σ-bound, metal ligandmaking the metal complex cationic and providing a charge-balancingnoncoordinating or weakly coordinating anion.

Aluminoxane and Aluminum Alkyl Activators

In one embodiment, alumoxane activators are utilized as an activator inthe catalyst composition useful in the invention. Alumoxanes aregenerally oligomeric compounds containing —Al(R¹)—O— sub-units, where R¹is an alkyl group. Examples of alumoxanes include methylalumoxane (MAO),modified methylalumoxane (MMAO), ethylalumoxane and isobutylalumoxane.Alkylalumoxanes and modified alkylalumoxanes are suitable as catalystactivators, particularly when the abstractable ligand is a halide,alkoxide or amide. Mixtures of different alumoxanes and modifiedalumoxanes may also be used.

The activator compounds comprising Lewis-acid activators and inparticular alumoxanes are represented by the following general formulae:(R³—Al—O)_(p)  (11)R⁴(R⁵—Al—O)_(p)—AlR⁶ ₂  (12)(M′)^(m+)Q′_(m)  (13)

An alumoxane is generally a mixture of both the linear and cycliccompounds. In the general alumoxane formula, R³, R⁴, R⁵ and R⁶ are,independently a C₁-C₃₀ alkyl radical, for example, methyl, ethyl,propyl, butyl, pentyl, hexyl, heptyl, octyl, nonyl, decyl, and “p” is aninteger from 1 to about 50. Most preferably, R³, R⁴, R⁵ and R⁶ are eachmethyl and “p” is a least 4. When an alkyl aluminum halide or alkoxideis employed in the preparation of the alumoxane, one or more R³⁻⁶ groupsmay be halide or alkoxide. M′ is a metal or metalloid, and Q′ is apartially or fully fluorinated hydrocarbyl.

It is recognized that alumoxane is not a discrete material. A typicalalumoxane will contain free trisubstituted or trialkyl aluminum, boundtrisubstituted or trialkyl aluminum, arid alumoxane molecules of varyingdegree of oligomerization. Those methylalumoxanes most preferred containlower levels of trimethylaluminum. Lower levels of trimethylaluminum canbe achieved by reaction of the trimethylaluminum with a Lewis base or byvacuum distillation of the trimethylaluminum or by any other means knownin the art. It is also recognized that after reaction with thetransition metal compound, some alumoxane molecules are in the anionicform as represented by the anion in equations 4-6, thus for our purposesare considered “non-coordinating” anions.

For further description,,, see U.S. Pat. Nos. 4,665,208, 4,952,540,5,041,584, 5,091,352, 5,206,199, 5,204,419, 4,874,734, 4,924,018,4,908,463, 4,968,827, 5,329,032, 5,248,801, 5,23.5,081, 5,157,137,5,103,031 and EP 0 561 476 A1, EP0 279 586 B1, EP0 516 476 A, EP0 594218 A1 and WO94/10180.

When the activator is an alumoxane (modified or unmodified), someembodiments select the maximum amount of activator at a 5000-fold molarexcess Al/M over the catalyst precursor (per metal catalytic site). Theminimum activator-to-catalyst-precursor is a 1:1 molar ratio.

Alumoxanes may be produced by the hydrolysis of the respectivetrialkylaluminum compound. MMAO may be produced by the hydrolysis oftrimethylaluminum and a higher trialkylaluminum such astriisobutylaluminum. MMAO's are generally more soluble in aliphaticsolvents and more stable during storage. There are a variety of methodsfor preparing alumoxane and modified alumoxanes, non-limiting examplesof which are described in U.S. Pat. Nos. 4,665,208, 4,952,540,5,091,352, 5,206,199, 5,204,419, 4,874,734, 4,924,018, 4,908,463,4,968,827, 5,308,815, 5,329,032, 5,248,801, 5,235,081, 5,157,137,5,103,031, 5,391,793, 5,391,529, 5,693,838, 5,731,253, 5,731,451,5,744,656, 5,847,177, 5,854,166, 5,856,256 and 5,939,346 and Europeanpublications EP-A-0 561 476, EP-B1-0 279 586, EP-A-0 594-218 and EP-B1-0586 665, and PCT publications WO 94/10180 and WO 39/15534, all of whichare herein fully incorporated by reference. It may be preferable to usea visually clear methylalumoxane. A cloudy or gelled alumoxane can befiltered to produce a clear solution or clear alumoxane can be decantedfrom the cloudy solution. Another alumoxane is a modified methylalumnoxane (MMAO) cocatalyst type 3A (commercially available from AkzoChemicals, Inc. under the trade name Modified Methylalumoxane type 3A,covered under patent number U.S. Pat. No. 5,041,584).

Aluminum alkyl or organoaluminum compounds which may be utilized asactivators (or scavengers) include trimethylaluminum, triethylaluminum,triisobutylaluminuni, tri-n-hexylaluminum, tri-n-octylaluminum and thelike.

Ionizing Activators

It is within the scope of this invention to use an ionizing orstoichiometric activator, neutral or ionic, such as tri(n-butyl)ammoniumtetrakis (pentafluorophenyl)boron, a trisperfluorophenyl boron metalloidprecursor or a trisperfluoronaphtyl boron metalloid precursor,polyhalogenated heteroborane anions (WO 98/43983), boric acid (U.S. Pat.No. 5,942,459) or combination thereof. It is also within the scope ofthis invention to use neutral or ionic activators alone or incombination with alumoxane or modified alumoxane activators.

Examples of neutral stoichiometric activators include tri-substitutedboron, tellurium, aluminum, gallium and indium or mixtures thereof. Thethree substituent groups are each independently selected from alkyls,alkenyls, halogen, substituted alkyls, aryls, arylhalides, alkoxy andhalides. Preferably, the three groups are independently selected fromhalogen, mono or multicyclic (including halosubstituted) aryls, alkytls,and alkenyl compounds and mixtures thereof, preferred are alkenyl groupshaving 1 to 20 carbon atoms, alkyl groups having 1 to 20 carbon atoms,alkoxy groups having 1 to 20 carbon atoms and aryl groups having 3 to 20carbon atoms (including substituted aryls). More preferably, the threegroups are alkyls having 1 to 4 carbon groups, phenyl, napthyl ormixtures thereof. Even more preferably, the three groups arehalogenated, preferably fluorinated, aryl groups. Most preferably, theneutral stoichiometric activator is trisperfluorophenyl boron ortrisperfluoronapthyl boron.

Ionic stoichiometric activator compounds may contain an active proton,or some other cation associated with, but not coordinated to, or onlyloosely coordinated to, the remaining [ion of the ionizing compound.Such compounds and the like are described in European publicationsEP-A-0 570 982, EP-A-0 520 732, EP-A-0 495 375, EP-B1-0 500 944, EP-A-0277 003 and EP-A-0 277 004, and U.S. Pat. Nos. 5,153,157, 5,198,401,5,066,741, 5,206,197, 5,241,025, 5,384,299 and 5,502,124 and U.S. patentapplication Ser. No. 08/285,380, filed Aug. 3, 1994, all of which areherein fully incorporated by reference.

Ionic catalysts can be preparedly reacting a transition metal compoundwith some neutral Lewis acids, such as B(C₆F₆)₃, which upon reactionwith the hydrolyzable ligand (X) of the transition metal compound formsan anion, such as ([B(C₆F₅)₃(X)]⁻), which stabilizes the cationictransition metal species generated by the reaction. The catalysts canbe, and preferably are, prepared with activator components which areionic compounds or compositions. However preparation of activatorsutilizing neutral compounds is also contemplated by this invention.

Compounds useful as an activator component in the preparation of theionic catalyst systems used in the process of this invention comprise acation, which is preferably a Bronsted acid capable of donating aproton, and a compatible non-coordinating anion which anion isrelatively large (bulky), capable of stabilizing the active catalystspecies (the Group 4 cation) which is formed when the two compounds arecombined and said anion will be sufficiently labile to be displaced byolefinic diolefinic and acetylenically unsaturated substrates or otherneutral Lewis bases such as ethers, nitrites and the like. Two classesof compatible non-coordinating anions have been disclosed in EPA 277,003and EPA 277,004 published 1988: 1) anionic coordination complexescomprising a plurality of lipophilic radicals covalently coordinated toand shielding a central charge-bearing metal or metalloid core, and 2)anions; comprising a plurality of boron atoms such as carboranes,metallacarboranes and boranes.

In a preferred embodiment, the stoichiometric activators include acation and an anion component, and may be represented by the followingformula:(L-H)_(d) ⁺(A^(d−))  (14)wherein L is an neutral Lewis base;

-   H is hydrogen;-   (L-H)⁺ is a Bronsted acid-   A^(d−) is a non-coordinating anion having, the charge d--   d is an integer from 1 to 3.

The cation component, (L-H)_(d) ⁺ may include Bronsted acids such asprotons or protonated Lewis bases or reducible Lewis acids capable ofprotonating or abstracting a moiety, such as an alkyl or aryl, from thebulky ligand metallocene containing transition metal catalyst precursor,resulting in a cationic transition metal species.

The activating cation (L-H)_(d) ⁺ may be a Bronsted acid, capable ofdonating a proton to the transition metal catalytic precursor resultingin a transition metal cation, including aminoniums, oxoniums,phosphoniums, silyliums, and mixtures thereof, preferably ammoniums ofmethylamine, aniline, dimethylamine, diethylamine, N-methylaniline,diphenylamine, trimethylamine, triethylamine, N,N-dimethylaniline,methyldiphenylamine, pyridine, p-bromo N,N-dimethylaniline,p-nitro-N,N-dimethylaniline, phosphoniums from triethylphosphine,triphenylphosphine, and diphenylphosphine, oxomiuns from ethers such asdimethyl ether diethyl (ether, tetrahydrofuran and dioxane, sulfoniumsfrom thioethers, such as diethyl thioethers and tetrahydrothiophene, andmixtures thereof. The activating cation (L-H)_(d) ⁺ may also be a moietysuch as silver, tropylium, carbeniums, ferroceniums and mixtures,preferably carboniums and ferroceniums. Most preferably (L-H)_(d) ⁺ istriphenyl carbonium.

The anion component Ad- include those having the formula[M^(k+)Q_(n)]^(d−) wherein k is an integer from 1 to 3; n is an integerfrom 2-6; n−k=d; M is an element selected from Group 13 of the PeriodicTable of the Elements, preferably boron or aluminum, and Q isindependently a hydride, bridged or unbridged dialkylamido, halide,alkoxide, aryloxide, hydrocarbyl, substituted hydrocarbyl, halocarbyl,substituted halocarbyl, and halosubstituted-hydrocarbyl radicals, said Qhaving up to 20 carbon atoms with the proviso that in not more than 1occurrence is Q a halide. Preferably, each Q is a fluorinatedhydrocarbyl group having 1 to 20 carbon atoms, more preferably each Q isa fluorinated aryl group, and most preferably each Q is a pentafluorylaryl group. Examples of suitable A^(d−) also include diboron compoundsas disclosed in U.S. Pat. No. 5,447,895, which is fully incorporatedherein by reference.

Illustrative, but not limiting examples of boron compounds which may beused as an activating cocatalyst in the preparation of the improvedcatalysts of this invention are tri-substituted ammonium salts such as:trimethylammonium tetraphenylborate, triethylammonium tetraphenylborate,tripropylammonium tetraphenylborate, tri(n-butyl)ammoniumtetraphenylborate, tri(t-butyl)ammonium tetraphenylborate,N,N-dimethylanilinium tetraphenylborate, N,N-diethylaniliniumtetraphenylborctte, N,N-dimethyl-(2,4,6-trimethylanilinium)tetraphenylborate, tropillium tetraphenylborate, triphenylcarbeniumtetraphenylborate, triphenylphosphonium tetraphenylboratetriethylsilylium tetraphenylborate,beinzene(diazonium)tetraphenylborate, trimethylammoniumtetrakis(pentafluorophenyl)borate, triethylammoniumtetrakis(pentafluorophenyl)borate, tripropylammoniumtetrakis(pentafluorophenyl)borate, tri(n-butyl)ammoniumtetrakis(pentafluorophenyl)borate, tri(sec-butyl)ammoniumtetrakis(pentafluorophenyl)borate, N,N-dimethylaniliniumtetrakis(pentafluorophenyl)borate, N,N-diethylaniliniumtetrakis(pentafluorophenyl)borate,N,N-dimethyl-(2,4,6-trimethylanilinium)tetrakis(pentafluorophenyl)borate, tropilliumtetrakis(pentafluorophenyl)borate, triphenylcarbeniumtetrakis(pentafluorophenyl)borate, triphenylphosphoniumtetrakis(pentafluorophenyl)borate, triethylsilyliumtetrakis(pentafluorophenyl)borate, benzene(diazonium)tetrakis(pentafluorophenyl)borate, trimethylammoniumtetrakis-(2,3,4,6-tetrafluorophenyl) borate, triethylammoniumtetrakis-(2,3,4,6-tetrafluorophenyl)borate, tripropylamnioniumtetrakis-(2,3,4,6-tetrafluorophenyl)borate, tri(n-butyl)ammoniumtetrakis-(2,3,4,6-tetrafluorophenyl)borate, dimethyl(t-butyl)ammoniumtetrakis-(2,3,4,6-tetrafluorophenyl)borate, N,N-dimethylaniliniumtetrakis-(2,3,4,6-tetrafluorophenyl)borate, N,N-diethylaniliniumtetrakis-(2,3,4,6-tetrafluorophenyl)borate,N,N-dimethyl-(2,4,6-trimethylanilinium)tetrakis-(2,3,4,6-tetrafluorophenyl)borate,tropillium tetrakis-(2,3,4,6-tetrafluorophenyl)borate,triphenylcarbenium tetrakis-(2,3,4,6-tetrafluorophenyl)borate,triphenylphosphonium tetrakis-(2,3,4,6-tetrafluorophenyl)borate,triethylsilylium tetrakis-(2,3,4,6-tetrafluorophenyl)borate,benzene(diazonium)tetrakis-(2,3,4,6-tetrafluorophenyl)borate,trimethylammonium tetrakis(perfluoronapthyl)borate, triethylammoniumtetrakis(perfluoronapthyl)borate, tripropylammoniumtetrakis(perfluoronapthyl)borate, tri(n-butyl)ammoniumtetrakis(perfluoronapthyl)borate, tri(t-butyl)ammoniumtetrakis(perfluoronapthyl)borate, N,N-dimethylaniliniumtetrakis(perfluoronapthyl)borate, N,N-diethylaniliniumtetrakis(perfluoronapthyl)borate,N,N-dimethyl-(2,4,6-trimethylanilinium)tetrakis(perfluoronapthyl)borate,tropillium tetrakis(perfluoronapthyl)borate, triphenylcarbeniumtetrakis(perfluoronapthyl)borate, triphenylphosphoniumtetrakis(perfluoronapthyl)borate, triethylsilyliumtetrakis(perfluoronapthyl)borate, benzene(diazonium)tetrakis(perfluoronapthyl)borate, trimethylammoniumtetrakis(perfluorobiphenyl)borate, triethylammoniumtetrakis(perfluorobiphenyl)borate, tripropylammoniumtetrakis(perfluorobiphenyl)borate, tri(n-butyl)ammoniumtetrakis(perfluorobiphenyl)borate, tri(t-butyl)ammoniumtetrakis(perfluorobiphenyl)borate, N,N-dimethylaniliniumtetrakis(perfluorobiphenyl)borate, N,N-diethylaniliniumtetrakis(perfluorobiphenyl)borate,N,N-dimethyl-(2,4,6-trimethylanilinium)tetrakis(perfluorobiphenyl)borate, tropilliumtetrakis(perfluorobiphenyl)borate, triphenylcarbeniumtetrakis(perfluorobiphenyl)borate, triphenylphosphoniumtetrakis(perfluorobiphenyl)borate, triethylsilyliumtetrakis(perfluorobiphenyl)borate, benzene(diazonium)tetrakis(perfluorobiphenyl)borate, trimethylammoniumtetrakis(3,5-bis(trifluoromethyl)phenyl)borate, triethylammoniumtetrakis(3,5-bis(trifluoromethyl)phenyl)borate, tripropylammoniumtetrakis(3,5-bis(trifluoromethyl)phenyl)borate, tri(n-butyl)ammoniumtetrakis(3,5-bis(trifluoromethyl)phenyl)borate, tri(t-butyl)ammoniumtetrakis(3,5-bis(trifluoromethyl)phenyl)borate, N,N-dimethylaniliniumtetrakis(3,5-bis(trifluoromethyl)phenyl)borate, N,N-diethylaniliniumtetrakis(3,5-bis(trifluoromethyl)phenyl)borate,N,N-dimethyl-(2,4,6-trimethylanilinium)tetrakis(3,5-bis(trifluoromethyl)phenyl)borate, tropilliumtetrakis(3,5-bis(trifluoromethyl)phenyl)borate, triphenylcarbeniumtetrakis(3,5-bis(trifluoromethyl)phenyl)borate, triphenylphosphoniumtetrakis(3,5-bis(trifluoromethyl)phenyl)borate, triethylsilyliumtetrakis(3,5-bis(trifluoromethyl)phenyl)borate, benzene(diazonium)tetrakis(3,5-bis(trifluoromethyl)phenyl)borate, and dialkyl ammoniumsalts such as: di-(i-propyl)ammonium tetrakis(pentafluorophenyl)borate,and dicyclohexylammonium tetrakis(pentafluorophenyl)borate; andadditional tri-substituted phosphonium salts such astri(o-tolyl)phosphonium tetrakis(pentafluorophenyl)borate, andtri(2,6-dimethylphenyl)phosphonium tetrakis(pentafluorophenyl)borate.

Most preferably, the ionic stoichiometric activator (L-H)_(d) ⁺(A^(d−))is N,N-dimethylanilinium tetra(perfluorophenyl)borate,N,N-dimethylanilinium tetrakis(perfluoronapthyl)borate,N,N-dimethylanilinium tetrakis(perfluorobiphenyl)borate,N,N(-dimethylanilinium tetrakis(3,5-bis(trifluoromethyl)phenyl)borate,triphenylcarbenium tetrakis(perfluoronapthyl)borate, triphenylcarbeniumtetrakis(perfluorobiphenyl)borate, triphenylcarbeniumtetrakis(3,5-bis(trifluoromethyl)phenyl)borate, or triphenylcarbeniumtetra(perfluorophenyl)borate.

In one embodiment, an activation method using ionizing ionic compoundsnot containing an active proton but capable of producing a bulky ligandmetallocene catalyst cation and their non-coordinating anion are alsocontemplated, and are described in EP-A-0 426 637, EP-A-0 573 403 andU.S. Pat. No. 5,387,568, which are all herein incorporated by reference.

The term “non-coordinating anion” (NCA) means an anion which either doesnot coordinate to said cation or which is only weakly coordinated tosaid cation thereby remaining sufficiently labile to be displaced by aneutral Lewis base. “Compatible” non-coordinating anions are those whichare not degraded to neutrality when the initially formed complexdecomposes. Further, the anion will not transfer an anionic substituentor fragment to the cation so as to cause it to form a neutral fourcoordinate metallocene compound and a neutral by-product from the anion.Non-coordinating anions useful in accordance with this invention arethose that are compatible, stabilize the metallocene cation in the senseof balancing its ionic charge at +1, yet retain sufficient lability topermit displacement by an ethylenically or acetylenically unsaturatedmonomer during polymerization. These types of cocatalysts sometimes usetri-isobutyl aluminum or tri-octyl aluminum as a scavenger.

Invention process also can employ cocatalyst compounds or activatorcompounds that are initially neutral Lewis acids but form a cationicmetal complex and a noncoordinating anion, or a zwitterionic complexupon reaction with the invention compounds. For example,tris(pentafluorophenyl) boron or aluminum act to abstract a hydrocarbylor hydride ligand to yield an invention cationic metal complex andstabilizing noncoordinating anion, see EP-A-0 427 697 and EP-A-0 520 732for illustrations of analogous Group-4 metallocene compounds. Also, seethe methods and compounds of EP-A-0 495 375. For formation ofzwitterionic complexes using analogous Group 4 compounds, see U.S. Pat.Nos. 5,624,878; 5,486,632; and 5,527,929.

When the cations of noncoordinating anion precursors are Bronsted acidssuch as protons or protonated Lewis bases (excluding water), orreducible Lewis acids such as ferrocenium or silver cations, or alkalior alkaline earth metal cations such as those of sodium, magnesium orlithium, the catalyst- precursor-to-activator molar ratio may be anyratio. Combinations of the described activator compounds may also beused for activation. For example, tris(perfluorophenyl) boron can beused with methylalumoxane.

Conventional-Type Cocatalysts (Activators)

Typically, conventional transition metal catalyst compounds excludingsome conventional-type chromium catalyst compounds are activated withone or more of the conventional cocatalysts which may be represented bythe formula:M³M⁴ _(v)X² _(c)R² _(b-c)  (15)wherein M³ is a metal from Group 1 to 3 and 12 to 13 of the PeriodicTable of Elements; M4 is a metal of Group 1 of the Periodic Table ofElements; v is a number from 0 to 1; each X² is any halogen; c is anumber from 0 to 3; each R² is a monovalent hydrocarbon radical orhydrogen; b is a number from 1 to 4; and wherein b minus c is atleast 1. Other conventional-type organometallic cocatalyst compounds forthe above conventional-type transition metal catalysts have the formulaM³R² _(k), where M³ is a Group IA, IIA, IIB or IIIA metal, such aslithium, sodium, beryllium, barium, boron, aluminum, zinc, cadmium, andgallium; k equals 1, 2 or 3 depending upon the vilency of M³ whichvalency in turn normally depends upon the particular Group to which M³belongs; and each R² may be any monovalent hydrocarbon radical.

Non-limiting examples of conventional-type organometallic cocatalystcompounds useful with the conventional-type catalyst compounds describedabove include methyllithium, butyllithium, dihexylmercury,butylmagnesium, diethylcadmium, bertzylpotassium, diethylzinc,tri-n-butylaluminum, diisobutyl ethylboron, diethylcadmium,di-n-butylzinc and tri-n-amylboron, and, in particular, the aluminumalkyls, such as tri-hexyl-aluminum, triethylaluminum, trimethylaluminum,and tri-isobutylaluminum. Other conventional-type cocatalyst compoundsinclude mono-organohalides and hydrides of Group 2 metals, and mono- ordi-organohalides and hydrides of Group 3 and 13 metals. Non-limitingexamples of such conventional-type cocatalyst compounds includedi-isobutylaluminum bromide, isobutylboron dichloride, methyl magnesiumchloride, ethylberyllium chloride, ethylcalcium bromide,di-isobutylaluminum hydride, methylcadmium hydride, diethylboronhydride, hexylberyllium hydride, dipropylboron hydride, octylmagnesiumhydride, butylzinc hydride, dichloroboron hydride, di-bromo-aluminumhydride and bromocadmium hydride. Conventional-type organometalliccocatalyst compounds are known to those in the art and a more completediscussion of these compounds may be found in U.S. Pat. Nos. 3,221,002and 5,093,415, which are herein fully incorporated by reference.

Additional Activators

Other activators include those described in PCT publication WO 98/07515such as tris (2,2′,2″-nonafluorobiphenyl) fluoroaluminate, whichpublication is fully incorporated herein by reference. Combinations ofactivators are also contemplated by the invention, for example,alumoxanes and ionizing activators in combinations, see for example,EP-B1 0 573 120, PCT publications WO 94/07928 and WO 95/14044 and U.S.Pat. Nos. 5,153,157 and 5,453,410 all of which are herein fullyincorporaled by reference. 1001861 Other suitable activators aredisclosed in WO 98/09996, incorporated herein by reference, whichdescribes activating bulky ligand metallocene catalyst compounds withperchlorates, periodates and iodates including their hydrates. WO98/30602 and WO 98/30603, incorporated by reference, describe the use oflithium (2,2′-bisphenyl-ditrimethylsilicate)•4THF as an activator for abulky ligand metallocene catalyst compound. WO 99/18135, incorporatedherein by reference, describes the use of organo-boron-aluminumactivators. EP-B 1-0 781 299 describes using a silylium salt incombination with a non-coordinating compatible anion. Also, methods ofactivation such as using radiation (see EP-B1-0 615 981 hereinincorporated by reference), electro-chemical oxidation, and the like arealso contemplated as activating methods for the purposes of renderingthe neutral bulky ligand metallocene catalyst compound or precursor to abulky ligand metallocene cation capable of polymerizing olefins. Otheractivators or methods for activating a bulky ligand metallocene catalystcompound are described in for example, U.S. Pat. Nos. 5,849,852,5,859,653 and 5,869,723 and WO 98/32775, WO 99/42467(dioctadecylmethylammonium-bis(tris(pentafluorophenyl)borane)benzimidazolide),which are herein incorporated by reference.

Another suitable ion firming, activating cocatalyst comprises a salt ofa cationic oxidizing agent and a noncoordinating, compatible anionrepresented by the formula:(OX^(e+))_(d)(A^(d−))_(e)  (16)wherein OX^(e+) is a cationic oxidizing agent having a charge of e+; eis an integer from 1 to 3; and A⁻, and d are as previously defined.Examples of cationic oxidizing agents include: ferrocenium,hydrocarbyl-substituted ferrocenium, Ag⁺, or Pb⁺². Preferred embodimentsof A^(d−) are those anions previously defined with respect to theBronsted acid containing activators, especiallytetrakis(pentafluorophenyl)borate.

It is within the scope of this invention that catalyst compounds can becombined one or more activators or activation methods described above.For example, a combination of activators; have been described in U.S.Pat. Nos. 5,153,157 and 5,453,410, European publication EP-B1 0 573 120,and PCT publications WO 94/07928 and WO 95/14044. These documents alldiscuss the use of an alumoxane and an ionizing activator with a bulkyligand metallocene catalyst compound.

The Choice of Transition Metal Catalyst Components

The catalyst system of this invention comprises two or more transitionmetal compounds as described above. At least one of the compounds mustbe capable of producing a crystalline poly-alpha-olefin, preferablyisotactic polypropylene or syndiotactic polypropylene, having acrystallinity of 40% or more. The other compound must be capable ofproducing an amorphous poly-alpha-olefin, preferably atacticpolypropylene, having a crystallinity of 20% or less.

The choice of transition metal component for the crystalline polymerfraction is a subset of the transition metal component of equations 8-9.This preferred component is illustrated in equation 17:

wherein A′, M, X₁ and X₂ are as previously defined. Substituents S″_(v)are independently defined as S″ in equations 8-9 where the subscript “v”denotes the carbon atom on the Cp-ring to which the substituent isbonded.

Preferably metallocene precursors for producing poly-alpha-olefinshaving enhanced isotactic character are those of Equation 17 whereS″_(v) are independently chosen such that the metallocene framework 1)has no plane of symmetry containing the metal center, and 2) has aC₂-axis of symmetry through the metal center. Such complexes, such asrac-Me₂Si(indenyl)₂ZrMe₂ and rac-Me₂Si(indenyl)₂HfMe₂ are well known inthe art and generally produce isotactic polymers with higher degrees ofstereoregularity than the less symmetric chiral systems. Likewiseanother preferred class of transition metal compounds that can produceisotactic polymers useful in this invention are thosemonocyclopentadienyl catalysts disclosed in U.S. Pat. No. 5,026,798,which is incorporated by reference herein.

Preferred chiral racemic metallocene compounds which, according to thepresent invention, provide catalyst systems which are specific to theproduction of isotactic poly-alpha-olefins include the racemic versionsof: dimethylsilylbis(indenyl)zirconium dichloride,dimethylsilylbis(indenyl)zirconium dimethyl,diphenylsilylbis(indenyl)zirconium dichloride,diphenylsilylbis(indenyl)zirconium dimethyl,methylphenylsilylbis(indenyl)zirconium dichloride,methylphenylsilylbis(indenyl)zirconium dimethyl,ethylenebis(indenyl)zirconium dichloride, ethylenebis(indenyl)zirconiumdimethyl, methylenebis(indenyl)zirconium dichloride,methylenebis(indenyl)zirconium dimethyl,dimethylsilylbis(indenyl)hafnium dichloride,dimethylsilylbis(indenyl)hafnium dimethyl,diphenylsilylbis(indenyl)hafnium dichloride, diphenylsilylbis(indenyl)hafnium dimethyl, methylphenylsilylbis(indenyl)hafnium dichloride,methylphenylsilylbis(indenyl)hafnium dimethyl,ethylenebis(indenyl)hafnium dichloride, ethylenebis(indenyl)hafniumdimethyl, methylenebis(indenyl)hafnium dichloride,methylenebis(indenyl)hafnium dimethyl,dimethylsilylbis(tetrahydroindenyl)zirconium dichloride,dimethylsilylbis(tetrahydroindenyl)zirconium dimethyl,diphenylsilylbis(tetrahydroindenyl)zirconium dichloride,diphenylsilylbis(tetrahydroindenyl)zirconium dimethyl,methylphenylsilylbis(tetrahydroindenyl)zirconium dichloride,methylphenylsilylbis(tetrahydroindenyl)zirconium dimethyl,ethylenebis(tetrahydroindenyl)zirconium dichloride,ethylenebis(tetrahydroindenyl)zirconium dimethyl,methylenebis(tetrahydroindenyl)zirconium dichloride,methylenebis(tetrahydroindenyl)zirconium dimethyl,dimethylsilylbis(tetrahydroindenyl)hafnium dichloride,dimethylsilylbis(tetrahydroindenyl)hafnium dimethyl,diphenylsilylbis(tetrahydroindenyl)hafnium dichloride,diphenylsilylbis(tetrahydroindenyl)hafnium dimethyl,methylphenylsilylbis(tetrahydroindenyl)hafnium dichloride,methylphenylsilylbis(tetrahydroindenyl)hafnium dimethyl,ethylenebis(tetrahydroindenyl)hafnium dichloride,ethylenebis(tetrahydroindenyl)hafnium dimethyl,methylenebis(tetrahydroindenyl)hafnium dichloride,methylenebis(tetrahydroindenyl)hafnium dimethyl,dimethylsilylbis(2-methylindenyl)zirconium dichloride,dimethylsilylbis(2-methylindenyl)zirconium dimethyl,diphenylsilylbis(2-methylindenyl)zirconium dichloride,diphenylsilylbis(2-methylindenyl)zirconium dimethyl,methylphenylsilylbis(2-methylindenyl)zirconium dichloride,methylphenylsilylbis(2-methylindenyl)zirconium dimethyl,ethylenebis(2-methylindenyl) zirconium dichloride,ethylenebis(2-methylindenyl)zirconium dimethyl,methylenebis(2-methylindenyl)zirconium dichloride,methylenebis(2-methylindenyl)zirconium dimethyl,dimethylsilylbis(2-methylindenyl)hafnium dichloride,dimethylsilylbis(2-methylindenyl)hafnium dimethyl,diphenylsilylbis(2-methylindenyl)hafnium dichloride,diphenylsilylbis(2-methylindenyl)hafnium dimethyl,methylphenylsilylbis(2-methylindenyl)hafnium dichloride,methylphenylsilylbis(2-methylindenyl)hafnium dimethyl,ethylenebis(2-methylindenyl)hafnium dichloride,ethylenebis(2-methylindenyl)hafnium dimethyl,methylenebis(2-methylindenyl)hafnium dichloride,methylenebis(2-methylindenyl)hafnium dimethyl,rac-dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dichloride,diphenylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl,diphenylsilylbis(2-methyl-4-phenylindenyl)zirconium dichloride,diphenylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl,methylphenylsilylbis(2-methyl-4-phenylindenyl)zirconium dichloride,methylphenylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl,ethylenebis(2-methyl-4-phenylindenyl)zirconium dichloride,ethylenebis(2-methyl-4-phenylindenyl)zirconium dimethyl,methylenebis(2-methyl-4-phenylindenyl)zirconium dichloride,methylenebis(2-methyl-4-phenylindenyl)zirconium dimethyl,dimethylsilylbis(2-methyl-4-phenylindenyl)hafnium dichloride,dimethylsilylbis(2-methyl-4-phenylindenyl)hafnium dimethyl,diphenylsilylbis(2-methyl-4-phenylindenyl)hafnium dichloride,diphenylsilylbis(2-methyl-4-phenylindenyl)hafnium dimethyl,methylphenylsilylbis(2-methyl-4-phenylindenyl)hafnium dichloride,methylphenylsilylbis(2-methyl-4-phenylindenyl)hafnium dimethyl,ethylenebis(2-methyl-4-phenylindenyl)hafnium dichloride,ethylenebis(2-methyl-4-phenylindenyl)hafnium dimethyl,methylenebis(2-methyl-4-phenylindenyl)hafnium dichloride,methylenebis(2-methyl-4-phenylindenyl)hafnium dimethyl,dimethylsilylbis(4,7-dimethylindenyl)zirconium dichloride,dimethylsilylbis(4,7-dimethylindenyl)zirconium dimethyl,diphenylsilylbis(4,7-dimethylindenyl)zirconium dichloride,diphenylsilylbis(4,7-dimethylindenyl)zirconium dimethyl,methylphenylsilylbis(4,7-dimethylindenyl)zirconium dichloride,methylphenylsilylbis(4,7-dimethylindenyl)zirconium dimethyl,ethylenebis(4,7-dimethylindenyl)zirconium dichloride,ethylenebis(4,7-dimethylindenyl)zirconium dimethyl,methylenebis(4,7-dimethylindenyl)zirconium dichloride,methylenebis(4,7-dimethylindenyl)zirconium dimethyl,dimethylsilylbis(4,7-dimethylindenyl)hafnium dichloride,dimethylsilylbis(4,7-dimethylindenyl)hafnium dimethyl,diphenylsilylbis(4,7-dimethylindenyl)hafnium dichloride,diphenylsilylbis(4,7-dimethylindenyl)hafnium dimethyl,methylphenylsilylbis(4,7-dimethylindenyl)hafnium dichloride,methylphenylsilylbis(4,7-dimethylindenyl)hafnium dimethyl,ethylenebis(4,7-dimethylindenyl)hafnium dichloride,ethylenebis(4,7-dimethylindenyl)hafnium dimethyl,methylenebis(4,7-dimethylindenyl)hafnium dichloride,methylenebis(4,7-dimethylindenyl)hafnium dimethyl,dimethylsilylbis(2-methyl-4-napthylindenyl)zirconium dichloride,dimethylsilylbis(2-methyl-4-napthylindenyl)zirconium dimethyl,diphenylsilylbis(2-methyl-4-napthylindenyl)zirconium dichloride,diphenylsilylbis(2-methyl-4-napthylindenyl)zirconium dimethyl,methylphenylsilylbis(2-methyl-4-napthylindenyl)zirconium dichloride,methylphenylsilylbis(2-methyl-4-napthylindenyl)zirconium dimethyl,ethylenebis(2-methyl-4-napthylindenyl)zirconium dichloride,ethylenebis(2-methyl-4-napthylindenyl)zirconium dimethyl,methylenebis(2-methyl-4-napthylindenyl)zirconium dichloride,methylenebis(2-methyl-4-napthylindenyl)zirconium dimethyl,dimethylsilylbis(2-methyl-4-napthylindenyl)hafnium dichloride,dimethylsilylbis(2-methyl-4-napthylindenyl)hafnium dimethyl,diphenylsilylbis(2-methyl-4-napthylindenyl)hafnium dichloride,diphenylsilylbis(2-methyl-4-napthylindenyl)hafnium dimethyl,methylphenylsilylbis(2-methyl-4-napthylindenyl)hafnium dichloride,methylphenylsilylbis(2-methyl-4-napthylindenyl)hafnium dimethyl,ethylenebis(2-methyl-4-napthylindenyl)hafnium dichloride,ethylenebis(2-methyl-4-napthylindenyl)hafnium dimethyl,methylenebis(2-methyl-4-napthylindenyl)hafnium dichloride,methylenebis(2-methyl-4-napthylindenyl)hafnium dimethyl,dimethylsilylbis(2,3-dimethylcyclopentadienyl)zirconium dichloride,dimethylsilylbis(2,3-dimethylcyclopentadienyl)zirconium dimethyl,diphenylsilylbis(2,3-dimethylcyclopentadienyl)zirconium dichloride,diphenylsilylbis(2,3-dimethylcyclopentadienyl)zirconium dimethyl,methylphenylsilylbis(2,3-dimethylcyclopentadienyl)zirconium dichloride,methylphenylsilylbis(2,3-dimethylcyclopentadienyl)zirconium dimethyl,ethylenebis(2,3-dimethylcyclopentadienyl)zirconium dichloride,ethylenebis(2,3-dimethylcyclopentadienyl)zirconium dimethyl,methylenebis(2,3-dimethylcyclopentadienyl)zirconium dichloride,methylenebis(2,3-dimethylcyclopentadienyl)zirconium dimethyl,dimethylsilylbis(2,3-dimethylcyclopentadienyl)hafnium dichloride,dimethylsilylbis(2,3-dimethylcyclopentadienyl)hafnium dimethyl,diphenylsilylbis(2,3-dimethylcyclopentadienyl)hafnium dichloride,diphenylsilylbis(2,3-dimethylcyclopentadienyl)hafnium dimethyl,methylphenylsilylbis(2,3-dimethylcyclopentadienyl)hafnium dichloride,methylphenylsilylbis(2,3-dimethylcyclopentadienyl)hafnium dimethyl,ethylenebis(2,3-dimethylcyclopentadienyl)hafnium dichloride,ethylenebis(2,3-dimethylcyclopentadienyl)hafnium dimethyl,methylenebis(2,3-dimethylcyclopentadienyl)hafnium dichloride,methylenebis(2,3-dimethylcyclopentadienyl)hafnium dimethyl,dimethylsilylbis(3-trimethylsilylcyclopentadienyl)zirconium dichloride,dimethylsilylbis(3-trimethylsilylcyclopentadienyl)zirconium dimethyl,diphenylsilylbis(3-trimethylsilylcyclopentadienyl)zirconium dichloride,diphenylsilylbis(3-trimethylsilylcyclopentadienyl)zirconium dimethyl,methylphenylsilylbis(3-trimethylsilylcyclopentadienyl)zirconiumdichloride,methylphenylsilylbis(3-trimethylsilylcyclopentadienyl)zirconiumdimethyl, ethylenebis(3-trimethylsilylcyclopentadienyl)zirconiumdichloride, ethylenebis(3-trimethylsilylcyclopentadienyl)zirconiumdimethyl, methylenebis(3-trimethylsilylcyclopentadienyl)zirconiumdichloride, methylenebis(3-trimethylsilylcyclopentadienyl)zirconiumdimethyl, dimethylsilylbis(3-trimethylsilylcyclopentadienyl)hafniumdichloride, dimethylsilylbis(3-trimethylsilylcyclopentadienyl)hafniumdimethyl, diphenylsilylbis(3-trimethylsilylcyclopentadienyl)hafniumdichloride, diphenylsilylbis(3-trimethylsilylcyclopentadienyl)hafniumdimethyl, methylphenylsilylbis(3-trimethylsilylcyclopentadienyl)hafniumdichloride,methylphenylsilylbis(3-trimethylsilylcyclopentadienyl)hafnium dimethyl,ethylenebis(3-trimethylsilylcyclopentadienyl)hafnium dichloride,ethylenebis(3-trimethylsilylcyclopentadienyl)hafnium dimethyl,methylenebis(3-trimethylsilylcyclopentadienyl)hafnium dichloride,methylenebis(3-trimethylsilylcyclopentadienyl)hafnium dimethyl,

-   dimethylsiladiyl(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-sec-butyl,    4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium dichloride;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-di-butylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dichloride;    dimethylsiladiyl(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-n-butyl,    4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium dimethyl;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dimethyl-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-(di-tbutylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-(di-tbutylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-n-propyl,    4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium dimethyl;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-sec-butyl,    4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium dimethyl;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)    ₂hafnium dimethyl;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-methyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)2zirconium    dichloride;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-methyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-methyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-sec-butyl,    4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium dichloride;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-methyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-n-butyl,    4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium dichloride;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-methyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-methyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)    ₂hafnium dimethyl;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)    ₂hafnium dimethyl;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-methyl,    4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium dimethyl;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-methyl,    4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium dimethyl;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-n-butyl,    4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium dimethyl;-   9-silafluorendiyl(2-iso-butyl,    4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium dimethyl;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)    ₂hafnium dichloride;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl-   dimethylsiladiyl(2-iso-propyl,    4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium dimethyl;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-isobutyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)    ₂hafnium dimethyl;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-tert-butyl,    4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium dimethyl;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-ethyl,    4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium dichloride;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-n-butyl,    4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium dichloride;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   dimethylsiladiyl(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   9-silafluorendiyl(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   dimethylsiladiyl(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-n-butyl,    4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium dimethyl;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylsiladiyl(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)2zirconium    dimethyl;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-sec-butyl,    4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium dimethyl;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   9-silafluorendiyl(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dichloride;-   9-silafluorendiyl(2-n-propyl,    4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium dimethyl;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dimethyl;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂hafnium    dimethyl;-   dimethylsiladiyl(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-    1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-sec-butyl,    4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylsiladiyl(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-n-butyl,    4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-n-propyl,4-[3′,5-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1    ,3-butadiene;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-tert-butyl,    4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-n-propyl,    4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1    ,3-butadiene;-   9-silafluorendiyl(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-iso-butyl,4-[3′,5″-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   9-silafluorendiyl(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-iso-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-sec-butyl,    4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium dichloride;-   dimethylamidoborane(2-tert-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-n-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-iso-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride-   dimethylamidoborane(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   dimethylamidoborane(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-iso-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-sec-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-tert-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-n-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-iso-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   dimethylamidoborane(2-methyl,4-[-3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-iso-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-sec-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-tert-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-n-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-iso-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-ethyl,4-[3′,5′di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl-   dimethylamidoborane(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   dimethylamidoborane(2-tert-butyl,    4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium dimethyl;-   diisopropylamidoborane(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-iso-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-sec-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-tert-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-ethyl,4-[′3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-n-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-iso-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride-   diisopropylamidoborane(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   diisopropylamidoborane(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-iso-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-sec-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-tert-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-n-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-iso-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   diisopropylamidoborane(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-iso-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-sec-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-tert-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;    diisopropylamidoborane(2-n-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;    diisopropylamidoborane(2-iso-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl-   diisopropylamidoborane(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-methyl,    4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium dimethyl;-   diisopropylamidoborane(2-ethyl,4-[1′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   diisopropylamidoborane(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-iso-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-iso-.butyl,    4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium dichloride;-   bis(trimethylsilyl)amidoborane(2-sec.-butyl,    4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium dichloride;-   bis(trimethylsilyl)amidoborane(2-tert-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-ethyl,    4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium dichloride;-   bis(trimethylsilyl)amidoborane(2-n-propyl,    4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium dichloride;-   bis(trimethylsilyl)amidoborane(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-n-butyl,    4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium dichloride;-   bis(trimethylsilyl)amidoborane(2-iso-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride-   bis(trimethylsilyl)amidoborane(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-n-butyl,    4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium dichloride;-   bis(trimethylsilyl)amidoborane(2-iso.-butyl,    4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium dichloride;-   bis(trimethylsilyl)amidoborane(2-sec-butyl,    4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium dichloride;-   bis(trimethylsilyl)amidoborane(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;    bis(trimethylsilyl)amidoborane(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-iso-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dichloride;-   bis(trimethylsilyl)amidoborane(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-    1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-n-propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-iso-.propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-iso.-butyl,    4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-sec-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-tert-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-ethyl,    4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-n-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-n-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-iso-butyl,    4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)²η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-iso-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-iso-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-methyl,    4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-iso.-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-n-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-sec-butyl,    4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂η⁴-1,4-diphenyl-1,3-butadiene;-   bis(trimethylsilyl)amidoborane(2-methyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-ethyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-n-propyl,    4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium dimethyl;-   bis(trimethylsilyl)amidoborane(2-iso-.propyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-n-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-iso.-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-sec-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-tert.-butyl,4-[3′,5′-di-tbutylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-ethyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-n-propyl,    4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium dimethyl;-   bis(trimethylsilyl)amidoborane(2-iso-propyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-n-butyl,    4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium dimethyl;-   bis(trimethylsilyl)amidoborane(2-iso-butyl,    4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium dimethyl;-   bis(trimethylsilyl)amidoborane(2-sec-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-tert-butyl,4-[3′,5′-bis-trifluoromethylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-ethyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-n-propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl-   bis(trimethylsilyl)amidoborane(2-iso-.propyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-n-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-iso-.butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-sec-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-tert-butyl,4-[3′,5′-di-iso-propylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-methyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-ethyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-n-propyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-iso-propyl,    4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium dimethyl;-   bis(trimethylsilyl)amidoborane(2-n-butyl,    4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium dimethyl;-   bis(trimethylsilyl)amidoborane(2-iso-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl;-   bis(trimethylsilyl)amidoborane(2-sec-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl; and-   bis(trimethylsilyl)amidoborane(2-tert-butyl,4-[3′,5′-di-phenylphenyl]indenyl)₂zirconium    dimethyl; and the like.

The most preferred species are the racemic versions of:dimethylsilylbis(indenyl)zirconium dichloride,dimethylsilylbis(indenyl)zirconium dimethyl,ethylenebis(indenyl)zirconium dichloride, ethylenebis(indenyl)zirconiumdimethyl, dimethylsilylbis(tetrahydorindenyl)zirconium dichloride,dimethylsilylbis(tetrahydorindenyl)zirconium dimethyl,ethylenebis(tetrahydorindenyl)zirconium dichloride,ethylenebis(tetrahydorindenyl)zirconium dimethyl,dimethylsilylbis(2-methylindenyl)zirconium dichloride,dimethylsilylbis(2-methylindenyl)zirconium dimethyl,ethylenebis(2-methylindenyl)zirconium dichloride,ethylenebis(2-methylindenyl)zirconium dimethyl,dimethylsilylbis(2-methyl-4 phenylindenyl)zirconium dichloride,dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl,ethylenebis(2-methyl-4-phenylindenyl)zirconium dichloride,ethylenebis(2-methyl-4-phenylindenyl)zirconium dimethyl,dimethylsilylbis(4,7-dimethylindenyl)zirconium dichloride,dimethylsilylbis(4,7-dimethylindenyl)zirconium dimethyl,ethylenebis(4,7-dimethylindenyl)zirconium dichloride,ethylenebis(4,7-dimethylindenyl)zirconium dimethyl,dimethylsilylbis(indenyl)hafnium dichloride,dimethylsilylbis(indenyl)hafnium dimethyl, ethylenebis(indenyl)hafniumdichloride, ethylenebis(indenyl)hafnium dimethyl,dimethylsilylbis(tetrahydorindenyl)hafnium dichloride,dimethylsilylbis(tetrahydorindenyl)hafnium dimethyl,ethylenebis(tetrahydorindenyl)hafnium dichloride,ethylenebis(tetrahydorindenyl)hafnium dimethyl,dimethylsilylbis(2-methylindenyl)hafnium dichloride,dimethylsilylbis(2-methylindenyl)hafnium dimethyl,ethylenebis(2-methylindenyl)hafnium dichloride,ethylenebis(2-methylindenyl)hafnium dimethyl,dimethylsilylbis(2-methyl-4-phenylindenyl)hafnium dichloride,dimethylsilylbis(2-methyl-4-phenylindenyl)hafnium dimethyl,ethylenebis(2-methyl-4-phenylindenyl)hafnium dichloride,ethylenebis(2-methyl-4-phenylindenyl)hafnium dimethyl,dimethylsilylbis(4,7-dimethylindenyl)hafnium dichloride,dimethylsilylbis(4,7-dimethylindenyl)hafnium dimethyl,ethylenebis(4,7-dimethylindenyl)hafnium dichloride, andethylenebis(4,7-dimethylindenyl)hafnium dimethyl.

Similarly, metallocene precursors providing tacticity control existwhere (A-Cp) is (Cp) (Cp*), both Cp and Cp* having substituents on thecyclopentadienyl rings of sufficient steric bulk to restrict rotation ofthe cyclopentadienyl ligands such that the aforementioned symmetryconditions are satisfied. Preferable chiral racemic metallocenes of thistype include bis(tricyclo[5.2.1.0^(2,6)]deca-2,5-dienyl)zirconium and-hafnium dimethyl,bis((1R)-9,9-dimethyltricyclo[6.1.1.0^(2,6)]deca-2,5-dienyl)zirconiumdimethyl, bis(tricyclo[5.2.1.0^(2,6)]deca-2,5,8-trienyl)zirconiumdimethyl, bis(tricyclo[5.2.2.0^(2,6)]undeca-2,5,8-trienyl)zirconium and-hafnium dimethyl and bis((1R,8R)-7,7,9,9-tetramethyl[6.1.1.0^(2,6)]deca-2,5-dienyl)zirconium and-hafnium dimethyl.

Preferably metallocene precursors for the production ofpoly-alpha-olefins having enhanced syndiotactic character are also thoseof Equation 17 where S″ are independently chosen such that the twoCp-ligands have substantially different steric bulk. In order to producea syndiotactic polymer the pattern of the groups substituted on theCp-rings is important. Thus, by steric difference or stericallydifferent as used herein, it is intended to imply a difference betweenthe steric characteristics of the Cp and Cp* rings that renders each tobe symmetrical With respect to the A bridging group but different withrespect to each other that controls the approach of each successivemonomer unit that is added to the polymer chain. The steric differencebetween the Cp and Cp* rings act to block the approaching monomer from arandom approach such that the monomer is added to the polymer chain inthe syndiotactic configuration.

Preferable metallocene precursors for the production of syndiotacticpolymers are those of Equation 17 where S″ are independently chosen suchthat 1) the steric difference between the two Cp-ligands is maximizedand 2) there remains a plane of symmetry through the metal center andthe C₁ and C_(1′) carbon atoms of the Cp-rings in Equation 17. Thus,complexes such as Me₂C(□⁵-C₅H₄)(1-fluorenyl)MMe₂ (where M=Ti, Zr, or Hf)which possess this symmetry are preferred, and generally produce thesyndiotactic polymer with higher degrees of stereoregularity thansimilar, but less symmetric, systems. Additionally, in the aboveequation, 1-fluorenyl may be substituted with 3,8-di-t-butylfluorenyl,octahydrofluorenyl or3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,10,10,11,11-octahydrodibenzo[b,h]fluorene.Because pre-catalysts of this type often lose there ability to controlthe stereoregularity of the polymer under high temperature reactionconditions, to insure higher crystallinity in the material requiresusing these catalysts at lower reactor temperatures, preferably attemperatures below 80° C.

Preferred catalysts that can produce the lower molecular weightisotactic polypropylene are those described in U.S. Pat. No. 5,120,867,which is incorporated by reference herein. Any mixture of catalysts,including supported catalysts, which can be used together in a singlereactor or in a series reactor configuration, that can also produce thedesired polypropylene can be utilized in this invention to produce thein situ blend. Preferred catalysts include cyclopentadienyl transitionmetals compounds and derivatives thereof used in conjunction with analumoxane and/or a compatible non-coordinating anion.

Additional preferred catalysts that produce crystalline polypropyleneare discussed in Chem. rev. 2000, 100, 1253-1345, which is incorporatedby reference herein.

The preferred choice of transition metal component for the amorphouspolymer fraction is the mi)no-cyclopentadienyl transition metalcomponent of equation 10 where y is equal to 1. This preferred componentis illustrated in equation 18:

where A′, J, S′, X₁, X₂, L′, z and w as are previously defined and M istitanium. Substituent S″_(v) is defined to be the same as S″ in equation10 where the subscript “v” denotes the carbon atom on thecyclopentadienyl ring to which the substituent is bonded and where therecan be zero, two or four substituents, S″, on the cyclopentadienyl ringprovided that the cyclopentadienyl ring is symmetrically substituted.Symmetrically substituted is defined to mean that the cyclopentadienylring is substituted in the 2 and 5 positions and/or 3 and 4 positionswith S″ groups that are of approximately of the same steric bulk.Typically the size of these S″ groups are within 2 carbons of eachother. Thus a cyclopentadienyl substituted at the 2 and the 5 positionswith methyl and ethyl respectively, or substituted at the 3 and the 4positions with hexyl and octyl, respectively, would be consideredsymmetric. Likewise, the cyclopentadienyl ring may be substituted at allfour sites with S″ groups and be considered symmetric as long as each ofthe symmetrical pairs are of similar steric bulk. Additionally, twoadjacent S″-groups in the 3 and 4 position may be linked to form a ringprovided that the new ring is also symmetrically substituted.

Catalyst systems of this type are known to impart 2,1-mistakes whenincorporating C3 and higher alpha-olefins. The pre-catalysts where S′ isbonded to the nitrogen ligand (J) via a 3° carbon (for example when S′is tert-butyl or 1-adamantyl) have fewer 2,1-mistakes then when S′ isbonded to the nitrogen ligand (J) via a 1° carbon (for example when S′is n-butyl, methyl, or benzyl) or 2° carbon (for example when S′ iscyclododecyl, cyclohexyl, or sec-butyl). The 2,1-mistakes in the polymerbackbone impart (CH₂)₂ units that can be beneficial to the polymerproperties. Polymers of this type, the characterization of such polymersand the catalyst systems used to produce such polymers are described inU.S. Pat. No. 5,723,560 and is incorporated herein by reference. LowerMw versions of such polymers can be produced by changing processcondition, for example, by increasing reactor temperature.

Preferred mono-cyclopentadienyl transition metal compounds which,according to the present invention, provide catalyst systems which arespecific to the production of atactic poly-alpha-olefins include:dimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(cyclohexylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(1-adamantylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(t-butylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(s-butylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(n-butylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(exo-2-norbornylamido)titaniumdichloride,diethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdichloride,diethylsilyl(tetramethylcyclopentadienyl)(exo-2-norbornylamido)titaniumdichloride,diethylsilyl(tetramethylcyclopentadienyl)(cyclohexylamido)titaniumdichloride,diethylsilyl(tetramethylcyclopentadienyl)(1-adamantylamido)titaniumdichloride,diethylsilyl(tetramethylcyclopentadienyl)(t-butylamido)titaniumdichloride,methylene(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdichloride,methylene(tetramethylcyclopentadienyl)(exo-2-norbornylamido)titaniumdichloride,methylene(tetramethylcyclopentadienyl)(cyclohexylamido)titaniumdichloride,methylene(tetramethylcyclopentadienyl)(1-adamantylamido)titaniumdichloride, methylene(tetramethylcyclopentadienyl)(t-butylamido)titaniumdichloride,ethylene(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdichloride,ethylene(tetramethylcyclopentadienyl)(exo-2-norbornylamido)titaniumdichloride,ethylene(tetramethylcyclopentadienyl)(cyclohexylamido)titaniumdichloride,ethylene(tetramethylcyclopentadienyl)(1-adamantylamido)titaniumdichloride, ethylene(tetramethylcyclopentadienyl)(t-butylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl,dimethylsilyl(tetramethylcyclopentadienyl)(cyclohexylamido)titaniumdimethyl,dimethylsilyl(tetramethylcyclopentadienyl)(1-adamantylamido)titaniumdimethyl,dimethylsilyl(tetramethylcyclopentadienyl)(t-butylamido)titaniumdimethyl,dimethylsilyl(tetramethylcyclopentadienyl)(s-butylamido)titaniumdimethyl,dimethylsilyl(tetramethylcyclopentadienyl)(n-butylamido)titaniumdimethyl,dimethylsilyl(tetramethylcyclopentadienyl)(exo-2-norbornylamido)titaniumdimethyl,diethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl,diethylsilyl(tetramethylcyclopentadienyl)(exo-2-norbornylamido)titaniumdimethyl,diethylsilyl(tetramethylcyclopentadienyl)(cyclohexylamido)titaniumdimethyl,diethylsilyl(tetramethylcyclopentadienyl)(1-adamantylamido)titaniumdimethyl,diethylsilyl(tetramethylcyclopentadienyl)(t-butylamido)titaniumdimethyl,methylene(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl,methylene(tetramethylcyclopentadienyl)(exo-2-norbornylamido)titaniumdimethyl,methylene(tetramethylcyclopentadienyl)(cyclohexylamido)titaniumdimethyl,methylene(tetramethylcyclopentadienyl)(1-adamantylamido)titaniumdimethyl, methylene(tetramethylcyclopentadienyl)(t-butylamido)titaniumdimethyl,ethylene(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl,ethylene(tetramethylcyclopentadienyl)(exo-2-norbornylamido)titaniumdimethyl, ethylene(tetramethylcyclopentadienyl)(cyclohexylamido)titaniumdimethyl,ethylene(tetramethylcyclopentadienyl)(1-adamantylamido)titaniumdimethyl, ethylene(tetramethylcyclopentadienyl)(t-butylamido)titaniumdimethyl,dimethylsilyl(2,5-dimethylcyclopentadienyl)(cyclododecylamido)titaniumdichloride,dimethylsilyl(2,5-dimethylcyclopentadienyl)(exo-2-norbornylamido)titaniumdichloride,dimethylsilyl(2,5-dimethylcyclopentadienyl)(cyclohexylamido)titaniumdichloride,dimethylsilyl(2,5-dimethylcyclopentadienyl)(1-adamantylamido)titaniumdichloride,dimethylsilyl(2,5-dimethylcyclopentadienyl)(t-butylamido)titaniumdichloride,dimethylsilyl(3,4-dimethylcyclopentadienyl)(cyclododecylamido)titaniumdichloride,dimethylsilyl(3,4-dimethylcyclopentadienyl)(exo-2-norbornylamido)titaniumdichloride,dimethylsilyl(3,4-dimethylcyclopentadienyl)(cyclohexylamido)titaniumdichloride,dimethylsilyl(3,4-dimethylcyclopentadienyl)(1-adamantylamido)titaniumdichloride,dimethylsilyl(3,4-dimethylcyclopentadienyl)(t-butylamido)titaniumdichloride,dimethylsilyl(2-ethyl-5-methylcyclopentadienyl)(cyclododecylamido)titaniumdichloride,dimethylsilyl(2-ethyl-5-methylcyclopentadienyl)(exo-2-norbornylamido)titaniumdichloride,dimethylsilyl(2-ethyl-5-methylcyclopentadienyl)(cyclohexylamido)titaniumdichloride,dimethylsilyl(2-ethyl-5-methylcyclopentadienyl)(1-adamantylamido)titaniumdichloride,dimethylsilyl(2-ethyl-5-methylcyclopentadienyl)(t-butylamido)titaniumdichloride,dimethylsilyl(3-ethyl-4-methylcyclopentadienyl)(cyclododecylamido)titaniumdichloride,dimethylsilyl(3-ethyl-4-methylcyclopentadienyl)(exo-2-norbornylamido)titaniumdichloride,dimethylsilyl(3-ethyl-4-methylcyclopentadienyl)(cyclohexylamido)titaniumdichloride,dimethylsilyl(3-ethyl-4-methylcyclopentadienyl)(1-adamantylamido)titaniumdichloride,dimethylsilyl(3-ethyl-4-methylcyclopentadienyl)(t-butylamido)titaniumdichloride,dimethylsilyl(2-ethyl-3-hexyl-5-methyl-4-octylcyclopentadienyl)(cyclododecylamido)titaniumdichloride,dimethylsilyl(2-ethyl-3-hexyl-5-methyl-4-octylcyclopentadienyl)(exo-2-norbornylamido)titaniumdichloride,dimethylsilyl(2-ethyl-3-hexyl-5-methyl-4-octylcyclopentadienyl)(cyclohexylamido)titaniumdichloride,dimethylsilyl(2-ethyl-3-hexyl-5-methyl-4-octylcyclopentadienyl)(1-adamantylamido)titaniumdichloride,dimethylsilyl(2-ethyl-3-hexyl-5-methyl-4-octylcyclopentadienyl)(t-butylamido)titaniumdichloride,dimethylsilyl(2-tetrahydroindenyl)(cyclododecylamido)titaniumdichloride,dimethylsilyl(2-tetrahydroindenyl)(exo-2-norbornylamido)titaniumdichloride, dimethylsilyl(2-tetrahydroindenyl)(cyclohexylamido)titaniumdichloride, dimethylsilyl(2-tetrahydroindenyl)(1-adamantylamido)titaniumdichloride, dimethylsilyl(2-tetrahydroindenyl)(t-butylamido)titaniumdichloride,dimethylsilyl(2,5-dimethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl,dimethylsilyl(2,5-dimethylcyclopentadienyl)(exo-2-norbornylamido)titaniumdimethyl,dimethylsilyl(2,5-dimethylcyclopentadienyl)(cyclohexylamido)titaniumdimethyl,dimethylsilyl(2,5-dimethylcyclopentadienyl)(1-adamantylamido)titaniumdimethyl,dimethylsilyl(2,5-(dimethylcyclopentadienyl)(t-butylamido)titaniumdimethyl,dimethylsilyl(3,4-dimethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl,dimethylsilyl(3,4-dimethylcyclopentadienyl)(exo-2-norbornylamido)titaniumdimethyl,dimethylsilyl(3,4-dimethylcyclopentadienyl)(cyclohexylamido)titaniumdimethyl,dimethylsilyl(3,4-dimethylcyclopentadienyl)(1-adamantylamido)titaniumdimethyl,dimethylsilyl(3,4-(dimethylcyclopentadienyl)(t-butylamido)titaniumdimethyl,dimethylsilyl(2-ethyl-5-methylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl,dimethylsilyl(2-ethyl-5-methylcyclopentadienyl)(exo-2-norbornylamido)titaniumdimethyl,dimethylsilyl(2-ethyl-5-methylcyclopentadienyl)(cyclohexylamido)titaniumdimethyl,dimethylsilyl(2-ethyl-5-methylcyclopentadienyl)(1-adamantylamido)titaniumdimethyl,dimethylsilyl(2-ethyl-5-methylcyclopentadienyl)(t-butylamido)titaniumdimethyl,dimethylsilyl(3-ethyl-4-methylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl,dimethylsilyl(3-ethyl-4-methylcyclopentadienyl)(exo-2-norbornylamido)titaniumdimethyl,dimethylsilyl(3-ethyl-4-methylcyclopentadienyl)(cyclohexylamido)titaniumdimethyl,dimethylsilyl(3-ethyl-4-methylcyclopentadienyl)(1-adamantylamido)titaniumdimethyl, dimethylsilyl(3-ethyl-4-methylcyclopentadienyl)(t-butylamido)titanium dimethyl,dimethylsilyl(2-ethyl-3-hexyl-5-methyl-4-octylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl,dimethylsilyl(2-ethyl-3-hexyl-5-methyl-4-octylcyclopentadienyl)(exo-2-norbornylamido)titaniumdimethyl,dimethylsilyl(2-ethyl-3-hexyl-5-methyl-4-octylcyclopentadienyl)(cyclohexylamido)titaniumdimethyl,dimethylsilyl(2-ethyl-3-hexyl-5-methyl-4-octylcyclopentadienyl)(1-adamantylamido)titaniumdimethyl,dimethylsilyl(2-ethyl-3-hexyl-5-methyl-4-octylcyclopentadienyl)(t-butylamido)titaniumdimethyl, dimethylsilyl(2-tetrahydroindenyl)(cyclododecylamido)titaniumdimethyl,dimethylsilyl(2-tetrahydroindenyl)(exo-2-norbornylamido)titaniumdimethyl, dimethylsilyl(2-tetrahydroindenyl)(cyclohexylamido)titaniumdimethyl, dimethylsilyl(2-tetrahydroindenyl)(1-adamantylamido)titaniumdimethyl, dimethylsilyl(2-tetrahydroindenyl)(t-butylamido)titaniumdimethyl and the like.

The most preferred species are:dimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(t-butylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(cyclohexylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(1-adamantylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(exo-2-norbornylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl,dimethylsilyl(tetramethylcyclopentadienyl)(t-butylamido)titaniumdimethyl,dimethylsilyl(tetramethylcyclopentadienyl)(cyclohexylamido)titaniumdimethyl,dimethylsilyl(tetramethylcyclopentadienyl)(1-adamantylamido)titaniumdimethyl, anddimethylsilyl(tetramethylcyclopentadienyl)(exo-2-norbornylamido)titaniumdimethyl.

Additionally, at higher reaction temperatures, some catalysts thatproduce syndiotactic poly-alpha-olefin at lower temperatures, willproduce virtually non-crystalline poly-alpha-olefins at highertemperatures. The choice of transition metal component for thisamorphous polymer fraction is a subset of the transition metal componentof equations 8-9. Preferred components of this type are illustrated inequation 19:

wherein A′, M, X₁ and X₂ are as previously defined. Substituents S″_(v)and S′″_(v) are independently defined as S″ in equations 8-9 where thesubscript “v” denotes the carbon atom on the Cp-ring or Flu-ring(fluorenyl-ring) to which the substituent is bonded.

Preferably metallocene precursors for producing poly-alpha-olefinshaving largely amorphous character (when used as catalysts under higherreactor temperature conditions) are those of Equation 19 where S′″_(v)are independently chosen such that the metallocene framework has a planeof symmetry containing the metal center and bisecting the Flu- andCp-rings. The A′ ligand need not be symmetrical—for exampledimethylsilyl or methylphenylsilyl will not effect the stereochemisty ofthe polymer produced. Substituent S′″_(v) is defined to be the same asS″ in equation 8-9 where the subscript “v” denotes the carbon atom onthe cyclopentadienyl ring to which the substituent is bonded and wherethere can be zero, two or four substituents, S′″, on thecyclopentadienyl ring provided that the cyclopentadienyl ring issymmetrically substituted. Symmetrically substituted is defined to meanthat the cyclopentadienyl ring is substituted in the 2 and 5 positionsand/or 3 and 4 positions with S′″ groups that are of approximately ofthe same steric bulk. Typically the size of these S′″ groups are within2 carbons of each other. Thus a cyclopentadienyl substituted at the 2and the 5 positions with methyl and ethyl respectively, or substitutedat the 3 and the 4 positions with hexyl and octyl, respectively, wouldbe considered symmetric. Likewise, the cyclopentadienyl ring may besubstituted at all four sites with S′″ groups and be consideredsymmetric as long as each of the symmetrical pairs are of similar stericbulk. Additionally, two adjacent S′″-groups in the 3 and 4 position maybe linked to form a ring provided that the new ring is alsosymmetrically substituted. Because of the distant placement of theS″_(v) substituents on the fluorenyl ring, these substitutents need notbe symmetrically placed on the fluorenyl ring. Hence, the fluorenyl ringmay be substituted with form 0-7 substituents that may be the same ordifferent. Two or more adjacent S″-groups may optionally be linked toform a ring.

Preferred metallocene transition metal compounds which, according to thepresent invention, provide catalyst systems which are specific to theproduction of amorphous or low crystallinity poly-alpha-olefins include:isopropylidene(cyclopentadienyl)(fluorenyl)zirconium dichloride,isopropylidene(cyclopentadienyl)(fluorenyl)zirconium dimethyl,methylene(cyclopentadienyl)(fluorenyl)zirconium dichloride,methylene(cyclopentadienyl)(fluorenyl)zirconium dimethyl,diphenylmethylene(cyclopentadienyl)(fluorenyl)zirconium dichloride,diphenylmethylene(cyclopentadienyl)(fluorenyl)zirconium dimethyl,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(fluorenyl)zirconiumdichloride,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(fluorenyl)zirconiumdimethyl,di(p-trimethylsilylphenyl)methylene(cyclopentadienyl)(fluorenyl)zirconiumdichloride,di(p-trimethylsilylphenyl)methylene(cyclopentadienyl)(fluorenyl)zirconiumdimethyl, diphenylsilyl(cyclopentadienyl)(fluorenyl)zirconiumdichloride, diphenylsilyl(cyclopentadienyl)(fluorenyl)zirconiumdimethyl, dimethylsilyl(cyclopentadienyl)(fluorenyl)zirconiumdichloride, dimethylsilyl(cyclopentadienyl)(fluorenyl)zirconiumdimethyl, methylphenylsilyl(cyclopentadienyl)(fluorenyl)zirconiumdichloride, methylphenylsilyl(cyclopentadienyl)(fluorenyl)zirconiumdimethyl, isopropylidene(cyclopentadienyl)(fluorenyl)hafnium dichloride,isopropylidene(cyclopentadienyl)(fluorenyl)hafnium dimethyl,methylene(cyclopentadienyl)(fluorenyl)hafnium dichloride,methylene(cyclopentadienyl)(fluorenyl)hafnium dimethyl,diphenylmethylene(cyclopentadienyl)(fluorenyl)hafnium dichloride,diphenylmethylene(cyclopentadienyl)(fluorenyl)hafnium dimethyl,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(fluorenyl)hafniumdichloride,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(fluorenyl)hafniumdimethyl,di(p-trimethylsilylphenyl)methylene(cyclopentadienyl)(fluorenyl)hafniumdichloride,di(p-trimethylsilylphenyl)methylene(cyclopentadienyl)(fluorenyl)hafniumdimethyl, diphenylsilyl(cyclopentadienyl)(fluorenyl)hafnium dichloride,diphenylsilyl(cyclopentadienyl)(fluorenyl)hafnium dimethyl,dimethylsilyl(cyclopentadienyl)(fluorenyl)hafnium dichloride,dimethylsilyl(cyclopentadienyl)(fluorenyl)hafnium dimethyl,methylphenylsilyl(cyclopentadienyl)(fluorenyl)hafnium dichloride,methylphenylsilyl(cyclopentadienyl)(fluorenyl)hafnium dimethyl,isopropylidene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconiumdichloride,isopropylidene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconiumdimethyl, methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconiumdichloride,methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconium dimethyl,diphenylmethylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconiumdichloride,diphenylmethylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconiumdimethyl, di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconium dichloride,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconiumdimethyl,di(p-trimethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconiumdichloride,di(p-trimethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconiumdimethyl,diphenylsilyl(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconiumdichloride,diphenylsilyl(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconiumdimethyl, dimethylsilyl(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconium dichloride,dimethylsilyl(cyclopentadienyl)(3,8-di-t- butylfluorenyl)zirconiumdimethyl,methylphenylsilyl(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconiumdichloride,methylphenylsilyl(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconiumdimethyl,isopropylidene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdichloride,isopropylidene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdimethyl, methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdichloride, methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdimethyl,diphenylmethylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdichloride,diphenylmethylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdimethyl,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdichloride,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdimethyl,di(p-trimethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdichloride,di(p-trimethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdimethyl,diphenylsilyl(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdichloride,diphenylsilyl(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdimethyl,dimethylsilyl(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdichloride,dimethylsilyl(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdimethyl,methylphenylsilyl(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdichloride,methylphenylsilyl(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdimethyl,isopropylidene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdichloride,isopropylidene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdimethyl,methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdichloride,methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdimethyl,diphenylmethylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdichloride,diphenylmethylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdimethyl,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdichloride,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdimethyl,di(p-trimethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdichloride,di(p-trimethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdimethyl,diphenylsilyl(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconium dichloride,diphenylsilyl(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdimethyl,dimethylsilyl(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdichloride,dimethylsilyl(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdimethyl,methylphenylsilyl(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdichloride,methylphenylsilyl(cyclopentadienyl)-3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdimethyl,isopropylidene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdichloride,isopropylidene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdimethyl,methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdichloride,methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdimethyl,diphenylmethylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdichloride,diphenylmethylene(cyclopentadienyl′)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdimethyl,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdichloride,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdimethyl,di(p-trimethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdichloride,di(p-trimethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdimethyl,diphenylsilyl(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdichloride,diphenylsilyl(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdimethyl,dimethylsilyl(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdichloride,dimethylsilyl(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdimethyl,methylphenylsilyl(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdichloride,methylphenylsilyl(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdimethyl, and the like.

The most preferred species are:di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconiumdichloride,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdichloride,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconiumdimethyl,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdimethyl,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdichloride,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdichloride,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdimethyl, anddi(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdimethyl.

Additionally, compounds of formula 20 may be used to produce theamorphous polymer fraction.

In this case, S″_(v) are independently chosen such that the metalloceneframework has a plane of symmetry that bisects M and A′. SubstituentsS″_(v) are independently defined to be the same as S″ in equation 8-9where the subscript “v” denotes the carbon atom on the cyclopentadienylring to which the substituent is bonded and where there can be zero tofour substituents, S″, on the cyclopentadienyl ring provided that thecyclopentadienyl ring is symmetrically substituted. Symmetricallysubstituted is defined to mean that the cyclopentadienyl ring issubstituted in the 2 and 2′ positions and/or 3 and 3′ positions and/or 4and 4′ positions and/or 5 and 5′ positions with S″ groups that are ofapproximately of the same steric bulk. Typically the size of these S″groups are within 2 carbons of each other. Thus a cyclopentadienylsubstituted at the 2 and the 2′ positions with methyl and ethylrespectively, or substituted at the 3 and the 3′ positions with hexyland octyl, respectively, would be considered symmetric. Likewise, thecyclopentadienyl ring may be substituted at all four sites with S″groups and be considered symmetric as long as each of the symmetricalpairs are of similar steric bulk. Additionally, two adjacent S″-groupsmay be linked to form a ring provided that the new ring is alsosymmetrically substituted. Such complexes such asmeso-Me₂Si(indenyl)₂ZrMe₂ meso-CH₂CH₂(indenyl)₂ZrCl₂ are well known inthe art and generally produce amorphous polymers useful in thisinvention.

Preferred meso-metallocene compounds which, according to the presentinvention, provide catalyst systems which are specific to the productionof amorphous poly- alpha-olefins include the meso versions of:dimethylsilylbis(indenyl)zirconium dichloride,dimethylsilylbis(indenyl)zirconium dimethyl,diphenylsilylbis(indenyl)zirconium dichloride,diphenylsilylbis(indenyl)zirconium dimethyl,methylphenylsilylbis(indenyl) zirconium dichloride,methylphenylsilylbis(indenyl)zirconium dimethyl,ethylenebis(indenyl)zirconium dichloride, ethylenebis(indenyl)zirconiumdimethyl, methylenebis(indenyl)zirconium dichloride,methylenebis(indenyl) zirconium dimethyl, dimethylsilylbis(indenyl)hafnium dichloride, dimethylsilylbis(indenyl)hafnium dimethyl,diphenylsilylbis(indenyl)hafnium dichloride,diphenylsilylbis(indenyl)hafnium dimethyl,methylphenylsilylbis(indenyl)hafnium dichloride,methylphenylsilylbis(indenyl)hafnium dimethyl,ethylenebis(indenyl)hafnium dichloride, ethylenebis(indenyl)hafniumdimethyl, methylenebis(indenyl)hafnium dichloride,methylenebis(indenyl)hafnium dimethyl,dimethylsilylbis(tetrahydroindenyl)zirconium dichloride,dimethylsilylbis(tetrahydroindenyl)zirconium dimethyl,diphenylsilylbis(tetrahydroindenyl)zirconium dichloride,diphenylsilylbis(tetrahydroindenyl)zirconium dimethyl,methylphenylsilylbis(tetrahydroindenyl)zirconium dichloride,methylphenylsilylbis(tetrahydroindenyl)zirconium dimethyl,ethylenebis(tetrahydroindenyl)zirconium dichloride,ethylenebis(tetrahydroindenyl)zirconium dimethyl,methylenebis(tetrahydroindenyl)zirconium dichloride,methylenebis(tetrahydroindenyl)zirconium dimethyl,dimethylsilylbis(tetrahydroindenyl)hafnium dichloride,dimethylsilylbis(tetrahydroindenyl)hafnium dimethyl,diphenylsilylbis(tetrahydroindenyl)hafnium dichloride,diphenylsilylbis(tetrahydroindenyl)hafnium dimethyl,methylphenylsilylbis(tetrahydroindenyl)hafnium dichloride,methylphenylsilylbis(tetrahydroindenyl)hafnium dimethyl,ethylenebis(tetrahydroindenyl)hafnium dichloride,ethylenebis(tetrahydroindenyl)hafnium dimethyl,methylenebis(tetrahydroindenyl)hafnium dichloride,methylenebis(tetrahydroindenyl)hafnium dimethyl,dimethylsilylbis(2-methylindenyl)zirconium dichloride,dimethylsilylbis(2-methylindenyl)zirconium dimethyl,diphenylsilylbis(2-methylindenyl)zirconium dichloride,diphenylsilylbis(2-methylindenyl)zirconium dimethyl,methylphenylsilylbis(2-methylindenyl)zirconium dichloride,methylphenylsilylbis(2-methylindenyl)zirconium dimethyl,ethylenebis(2-methylindenyl)zirconium dichloride,ethylenebis(2-methylindenyl)zirconium dimethyl,methylenebis(2-methylindenyl)zirconium dichloride,methylenebis(′-methylindenyl)zirconium dimethyl,dimethylsilylbis(2-methylindenyl)hafnium dichloride,dimethylsilylbis(2-methylindenyl)hafnium dimethyl,diphenylsilylbis(2-methylindenyl)hafnium dichloride,diphenylsilylbis(2-methylindenyl)hafnium dimethyl,methylphenylsilylbis(2-methylindenyl)hafnium dichloride,methylphenylsilylbis(2-methylindenyl)hafnium dimethyl,ethylenebis(2-methylindenyl)hafnium dichloride,ethylenebis(2-methylindenyl)hafnium dimethyl,methylenebis(2-methylindenyl)hafnium dichloride,methylenebis(2-methylindenyl)hafnium dimethyl,dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dichloride,diphenylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl,diphenylsilylbis(2-methyl-4-phenylindenyl)zirconium dichloride,diphenylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl,methylphenylsilylbis(2-methyl-4-phenylindenyl)zirconium dichloride,methylphenylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl,ethylenebis(2-methyl-4-phenylindenyl)zirconium dichloride,ethylenebis(2-methyl-4-phenylindenyl)zirconium dimethyl,methylenebis(2-methyl-4-phenylindenyl)zirconium dichloride,methylenebis(2-methyl-4-phenylindenyl)zirconium dimethyl,dimethylsilylbis(2-methyl-4-phenylindenyl)hafnium dichloride,dimethylsilylbis(2-methyl-4-phenylindenyl)hafnium dimethyl,diphenylsilylbis(2-methyl-4-phenylindenyl)hafnium dichloride,diphenylsilylbis(2-methyl-4-phenylindenyl)hafnium dimethyl,methylphenylsilylbis(2-methyl-4-phenylindenyl)hafnium dichloride,methylphenylsilylbis(2-methyl-4-phenylindenyl)hafnium dimethyl,ethylenebis(2-methyl-4-phenylindenyl)hafnium di(chloride,ethylenebis(2-methyl-4-phenylindenyl)hafnium dimethyl,methylenebis(2-methyl-4-phenylindenyl)hafnium dichloride,methylenebis(2-methyl-4-phenylindenyl)hafnium dimethyl,dimethylsilylbis(4,7-dimethylindenyl)zirconium dichloride,dimethylsilylbis(4,7-dimethylindenyl)zirconium dimethyl,diphenylsilylbis(4,7-dimethylindenyl)zirconium dichloride,diphenylsilylbis(4,7-dimethylindenyl)zirconium dimethyl,methylphenylsilylbis(4,7-dimethylindenyl)zirconium dichloride,methylphenylsilylbis(4,7-dimethylindenyl)zirconium dimethyl,ethylenebis(4,7-dimethylindenyl)zirconium dichloride,ethylenebis(4,7-dimethylindenyl)zirconium dimethyl,methylenebis(4,7-dimethylindenyl)zirconium dichloride,methylenebis(4,7-dimethylindenyl)zirconium dimethyl,dimethylsilylbis(4,7-dimethylindenyl)hafnium dichloride,dimethylsilylbis(4,7-dimethylindenyl)hafnium dimethyl,diphenylsilylbis(4,7-dimethylindenyl)hafnium dichloride,diphenylsilylbis(4,7-dimethylindenyl)hafnium dimethyl,methylphenylsilylbis(4,7-dimethylindenyl)hafnium dichloride,methylphenylsilylbis(4,7-dimethylindenyl)hafnium dimethyl,ethylenebis(4,7-dimethylindenyl)hafnium dichloride,ethylenebis(4,7-dimethylindenyl)hafnium dimethyl,methylenebis(4,7-dimethyl]indenyl)hafnium dichloride,methylenebis(4,7-dimethylindenyl)hafnium dimethyl, and the like.

The most preferred species are the racemic versions of:dimethylsilylbis(indenyl)zirconium dichloride,dimethylsilylbis(indenyl)zirconium dimethyl,ethylenebis(indenyl)zirconium dichloride, ethylenebis(indenyl)zirconiumdimethyl, dimethylsilylbis(indenyl) hafnium dichloride,dimethylsilylbis(indenyl)hafnium dimethyl, ethylenebis(indenyl)hafniumdichloride, ethylenebis(indenyl)hafnium dimethyl,dimethylsilylbis(tetrahydroindenyl)zirconium dichloride,dimethylsilylbis(tetrahydroindenyl)zirconium dimethyl,ethylenebis(tetrahydroindenyl)zirconium dichloride,ethylenebis(tetrahydroindenyl)zirconium dimethyl,dimethylsilylbis(tetrahydroindenyl)hafnium dichloride,dimethylsilylbis(tetrahydroindenyl)hafnium dimethyl,ethylenebis(tetrahydroindenyl)hafnium dichloride,ethylenebis(tetrahydroindenyl)hafnium dimethyl,dimethylsilylbis(2-methylindenyl)zirconium dichloride,dimethylsilylbis(2-methylindenyl)zirconium dimethyl,ethylenebis(2-methylindenyl)zirconium dichloride,ethylenebis(2-methylindenyl)zirconium dimethyl,dimethylsilylbis(2-methylindenyl)hafnium dichloride,dimethylsilylbis(2-methylindenyl)hafnium dimethyl,ethylenebis(2-methylindenyl)hafnium dichloride, andethylenebis(2-methylindenyl)hafnium dimethyl

When two transition metal compound based catalysts are used in onereactor as a mixed catalyst system, the two transition metal compoundsshould be chosen such that the two are compatible. A simple screeningmethod such as by ¹H or ¹³C NMR, known to those of ordinary skill in theart, can be used to determine which transition metal compounds arecompatible.

It is preferable to use the same activator for the transition metalcompounds, however, two different activators, such as a non-coordinatinganion activator and an alumoxane, can be used in combination. If one ormore transition metal compounds contain an X₁ or X₂ ligand which is nota hydride, hydrocarbyl, or substituted hydrocarbyl, then the alumoxaneshould be contacted with the transition metal compounds prior toaddition of the non-coordinating anion activator.

Particularly preferred combinations of transition metal compoundsinclude:

-   -   (1) Me₂Si(Me₄C₅)(N-c-C₁₂H₂₃)TiCl₂ and        rac-Me₂Si(2-Me-4-PhInd)₂ZrCl₂        (2-Me-4-PhInd=2-methyl-4-phenylindenyl, c-Cl₂H₂₃=cyclododecyl,        Me₄C₅- tetramethylcyclopentadienyl) activated with an alumoxane,        such as methylalumoxane or modified methylalumoxane;    -   (2) Me₂Si(Me₄C₅)(N-c-C₁₂H₂₃)TiMe₂ and        rac-Me₂Si(2-Me-4-PhInd)₂ZrMe₂ activated with a non-coordinating        anion activator, such as N,N-dimethylanilinium        tetrakis(pentaflourophenyl)boron or triphenylcarbonium        tetrakis(pentaflourophenyl)boron;    -   (3) Me₂Si(Me₄C₅)(N-c-C₁₂H₂₃)TiCl₂ and rac-Me₂Si(2-MeInd)₂ZrCl₂        (2-MeInd=2-methyl-indenyl) activated with an alumoxane, such as        methylalumoxane or modified methylalumoxane;

-   (4) Me₂Si(Me₄C₅)(N-c-C₁₂H₂₃)TiMe₂ and rac-Me₂Si(2-MeInd)₂ZrMe₂    activated with a non-coordinating anion activator, such as    N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or    triphenylcarbonium tetrakis(pentaflourophenyl)boron;

-   (5) Me₂Si(Me₄C₅)(N-1-adamantyl)TiCl₂ and    rac-Me₂Si(2-Me-4-PhInd)₂ZrCl₂ activated with an alumoxane, such as    methylalumoxane or modified methylalumoxane;    -   (6) Me₂Si(Me₄C₅)(N-1-adamantyl)TiMe₂ and        rac-Me₂Si(2-Me-4-PhInd)₂ZrMe₂ activated with a non-coordinating        anion activator, such as N,N-dimethylanilinium        tetrakis(pentaflourophenyl)boron or triphenylcarbonium        tetrakis(pentaflourophenyl)boron;    -   (7) Me₂Si(Me₄C₅)(N-1-adamantyl)TiCl₂ and        rac-Me₂Si(2-MeInd)₂ZrCl₂ activated with an alumoxane, such as        methylalumoxane or modified methylalumoxane;    -   (8) Me₂Si(Me₄C₅)(N-1-adamantyl)TiMe₂ and        rac-Me₂Si(2-MeInd)₂ZrMe₂ activated with a non-coordinating anion        activator, such as N,N-dimethylanilinium        tetrakis(pentaflourophenyl)boron or triphenylcarbonium        tetrakis(pentaflourophenyl)boron;    -   (9) Me₂Si(Me₄C₅)(N-t-butyl)TiCl₂ and        rac-Me₂Si(2-Me-4-PhInd)₂ZrCl₂ activated with an alumoxane, such        as methylalumoxane or modified methylalumoxane;    -   (10) Me₂Si(Me₄C₅)(N-t-butyl)TiMe₂ and        rac-Me₂Si(2-Me-4-PhInd)₂ZrMe₂ activated with a non-coordinating        anion activator, such as N,N-dimethylamilinium        tetrakis(pentaflourophenyl)boron or triphenylcarbonium        tetrakis(pentaflourophenyl)boron;    -   (11) Me₂Si(Me₄C₅)(N-t-butyl)TiCl₂ and rac-Me₂Si(2-MeInd)        activated with an alumoxane, such as methylalumoxane or modified        methylalumoxane;    -   (12) Me₂Si(Me₄C₅)(N-t-butyl)TiMe₂ and rac-Me₂Si(2-MeInd)₂ZrMe₂        activated with a non-coordinating anion activator, such as        N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or        triphenylcarbonium tetrakis(pentaflourophenyl)boron;    -   (13) Me₂Si(Me₄C₅)(N-exo-norbornyl)TiCl₂ and        rac-Me₂Si(2-Me-4-PhInd)₂ZrCl₂ activated with an alumoxane, such        as methylalumoxane or modified methylalumoxane;    -   (14) Me₂Si(Me₄C₅)(N-exo-norbornyl)TiMe₂ and        rac-Me₂Si(2-Me-4-PhInd)₂ZrMe₂ activated with a non-coordinating        anion activator, such as N,N-dimethylanilinium        tetrakis(pentaflourophenyl)boron or triphenylcarbonium        tetrakis(pentaflourophenyl)boron;    -   (15) Me₂Si(Me₄C₅)(N-exo-norbornyl)TiCl₂ and        rac-Me₂Si(2-MeInd)₂ZrCl₂ activated with an alumoxane, such as        methylalumoxane or modified methylalumoxane;    -   (16) Me₂Si(Me₄C₅)(N-exo-norbornyl)TiMe₂ and        rac-Me₂Si(2-MeInd)₂ZrMe₂ activated with a non-coordinating anion        activator, such as N,N-dimethylanilinium        tetrakis(pentaflourophenyl)boron or triphenylcarbonium        tetrakis(pentaflourophenyl)boron;    -   (17) (p-Et₃SiPh)₂C(Cp)(3,8-di-t-BuFlu)HfCl₂ and        rac-Me₂Si(2-Me-4-PhInd)₂ZrCl₂        (3,8-di-t-BuFlu=3,8-di-tert-butylfluorenyl, Cp=cyclopentadienyl)        activated with an alumoxane, such as methylalumoxane or modified        methylalumoxane;    -   (18) (p-Et₃SiPh)₂C(Cp)(3,8-di-t-BuFlu)HfMe₂ and        rac-Me₂Si(2-Me-4-PhInd)₂ZrMe₂ activated with a non-coordinating        anion activator, such as N,N-dimethylanilinium        tetrakis(pentaflourophenyl)boron or triphenylcarbonium        tetrakis(pentaflourophenyl)boron;    -   (19) (p-Et₃SiPh)₂C(Cp)(3,8-di-t-BuFlu)HfCl₂ and        rac-Me₂Si(2-MeInd)₂ZrCl₂ activated with an alumoxane, such as        methylalumoxane or modified methylalumoxane;    -   (20) (p-Et₃SiPh)₂C(Cp)(3,8-di-t-BuFlu)HfMe₂ and        rac-Me₂Si(2-MeInd)₂ZrMe₂ activated with a non-coordinating anion        activator, such as N,N-dimethylanilinium        tetrakis(pentaflourophenyl)boron or triphenylcarbonium        tetrakis(pentaflourophenyl)boron;    -   (21) meso-CH₂CH₂(Ind)₂ZrCl₂ and rac-Me₂Si(H₄Ind)₂ZrCl₂        (Ind=indenyl, H₄Ind=tetrahydroindenyl) activated with an        alumoxane, such as methylalumoxane or modified methylalumoxane;    -   (22) meso-CH₂CH₂(Ind)₂ZrMe₂ and rac-Me₂Si(H₄Ind)₂ZrMe₂ activated        with a non-coordinating anion activator, such as        N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or        triphenylcarbonium tetrakis(pentaflourophenyl)boron;

-   (23) meso-CH₂CH₂(Ind)₂ZrCl₂ and rac-Me₂Si(2-MeInd)₂ZrCl₂ activated    with an alumoxane, such as methylalumoxane or modified    methylalumoxane;    -   (24) meso-CH₂CH₂(Ind)₂ZrMe₂ and rac-Me₂Si(2-MeInd)₂ZrMe₂        activated with a non-coordinating anion activator, such as        N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or        triphenylcarbonium tetrakis(pentaflourophenyl)boron;

-   (25) meso-Me₂Si(Ind)₂ZrCl₂ and rac-Me₂Si(H₄Ind)₂ZrCl₂ activated with    an alumoxane, such as methylalumoxane or modified methylalumoxane;    -   (26) meso-Me₂Si(Ind)₂ZrMe₂ and rac-Me₂Si(H₄Ind)₂ZrMe₂ activated        with a non-coordinating anion activator, such as        N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or        triphenylcarbonium tetrakis(pentaflourophenyl)boron;    -   (27) meso-Me₂Si(Ind)₂ZrCl₂ and rac-Me₂Si(2-MeInd)₂ZrCl₂        activated with an alumoxane, such as methylalumoxane or modified        methylalumoxane;    -   (28) meso-Me₂Si(Ind)₂ZrMe₂ and rac-Me₂Si(2-MeInd)₂ZrMe₂        activated with a non-coordinating anion activator, such as        N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or        triphenylcarbonium tetrakis(pentaflourophenyl)boron;    -   (29) meso-Me₂Si(2-MeInd)₂ZrCl₂ and rac-Me₂Si(2-Me-4-PhInd)₂ZrCl₂        activated with an alumoxane, such as methylalumoxane or modified        methylalumoxane;    -   (30) meso-Me₂Si(2-MeInd)₂ZrMe₂ and rac-Me₂Si(2-Me-4-PhInd)₂ZrMe₂        activated with a non-coordinating anion activator, such as        N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or        triphenylcarbonium tetrakis(pentaflourophenyl)boron;    -   (31) meso-Me₂Si(2-MeInd)₂ZrCl₂ and rac-Me₂Si(2-MeInd)₂ZrCl₂        activated with an alumoxane, such as methylalumoxane or modified        methylalumoxane;    -   (32) meso-Me₂Si(2-MeInd)₂ZrMe₂ and rac-Me₂Si(2-MeInd)₂ZrMe₂        activated with a non-coordinating anion activator, such as        N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or        triphenylcarbonium tetrakis(pentaflourophenyl)boron;    -   (33) meso-CH₂CH₂(2-MeInd)₂ZrCl₂ and        rac-Me₂Si(2-Me-4-PhInd)₂ZrCl₂ activated with an alumoxane, such        as methylalumoxane or modified methylalumoxane;    -   (34) meso-CH₂CH₂(2-MeInd)₂ZrMe₂ and        rac-Me₂Si(2-Me-4-PhInd)₂ZrMe₂ activated with a non-coordinating        anion activator, such as N,N-dimethylanilinium        tetrakis(pentaflourophenyl)boron or triphenylcarbonium        tetrakis(pentaflourophenyl)boron;    -   (35) meso-CH₂CH₂(2-MeInd)₂ZrCl₂ and rac-Me₂Si(2-MeInd)₂ZrCl₂        activated with an alumoxane, such as methylalumoxane or modified        methylalumoxane;    -   (36) meso-CH₂CH₂(2-MeInd)₂ZrMe₂ and rac-Me₂Si(2-MeInd)₂ZrMe₂        activated with a non-coordinating anion activator, such as        N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or        triphenylcarbonium tetrakis(pentaflourophenyl)boron;    -   (37) meso-Me₂Si(2-Me-4-′PhInd)₂ZrCl₂ and        rac-Me₂Si(2-Me-4-PhInd)₂ZrCl₂ activated with an alumoxane, such        as methylalumoxane or modified methylalumoxane;    -   (38) meso-Me₂Si(2-Me-4-′PhInd)₂ZrMe₂ and        rac-Me₂Si(2-Me-4-PhInd)₂ZrMe₂ activated with a non-coordinating        anion activator, such as N,N-dimethylanilinium        tetrakis(pentaflourophenyl)boron or triphenylcarbonium        tetrakis(pentaflourophenyl)boron;    -   (39) meso-CH₂CH₂(2-Me-4-PhInd)₂ZrCl₂ and        rac-CH₂CH₂(2-Me-4-PhInd)₂ZrCl₂ activated with an alumoxane, such        as methylalumoxane or modified methylalumoxane;    -   (40) meso-CH₂CH₂(2-Me-4-PhInd)₂ZrMe₂ and        rac-CH₂CH₂(2-Me-4-PhInd)₂ZrMe₂ activated with a non-coordinating        anion activator, such as N,N-dimethylanilinium        tetrakis(pentaflourophenyl)boron or triphenylcarbonium        tetrakis(pentaflourophenyl)boron;    -   (41) meso-CH₂CH₂(2-MeInd)₂ZrCl₂ and rac-CH₂CH₂(2-MePhInd)₂ZrCl₂        activated with an alumoxane, such as methylalumoxane or modified        methylalumoxane;    -   (42) meso-CH₂CH₂(2-MeInd)₂ZrMe₂ and rac-CH₂CH₂(2-MeInd)₂ZrMe₂        activated with a non-coordinating anion activator, such as        N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or        triphenylcarbonium tetrakis(pentaflourophenyl)boron;    -   (43) meso-CH₂CH₂(Ind)₂ZrCl₂ and rac-CH₂CH₂(Ind)₂ZrCl₂ activated        with an alumoxane, such as methylalumoxane or modified        methylalumoxane;    -   (44) meso-CH₂CH₂(Ind)₂ZrMe₂ and rac-CH₂CH₂(Ind)₂ZrMe₂ activated        with a non-coordinating anion activator, such as        N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or        triphenylcarbonium tetrakis(pentaflourophenyl)boron;    -   (45) meso-Me₂Si(Ind)₂ZrCl₂ and rac-Me₂Si(Ind)₂ZrCl₂ activated        with an alumoxane, such as methylalumoxane or modified        methylalumoxane;    -   (46) meso-Me₂Si(Ind)₂ZrMe₂ and rac-Me₂Si(Ind)₂ZrMe₂ activated        with a non-coordinating anion activator, such as        N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or        triphenylcarbonium tetrakis(pentaflourophenyl)boron;    -   (47) meso-CH₂CH₂(Ind)₂ZrCl₂ and rac-CH₂CH₂(4,7-Me₂Ind)₂ZrCl₂        (4,7-Me₂Ind=4,7-dimethylindenyl) activated with an alumoxane,        such as methylalumoxane or modified methylalumoxane;    -   (48) meso-CH₂CH₂(Ind)₂ZrMe₂ and rac-CH₂CH₂(4,7-Me₂Ind)₂ZrMe₂        activated with a non-coordinating anion activator, such as        N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or        triphenylcarbonium tetrakis(pentaflourophenyl)boron;    -   (49) meso-Me₂Si(Ind)₂ZrCl₂ and rac-CH₂CH₂(4,7-Me₂Ind)₂ZrCl₂        activated with an alumoxane, such as methylalumoxane or modified        methylalumoxane;    -   (50) meso-Me₂Si(Ind)₂ZrMe₂ and rac-CH₂CH₂(4,7-Me₂Ind)₂ZrMe₂        activated with a non-coordinating anion activator, such as        N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or        triphenylcarbonium tetrakis(pentaflourophenyl)boron;    -   (51) meso-CH₂CH₂(2-MeInd)₂ZrCl₂ and rac-CH₂CH₂(4,7-Me₂Ind)₂ZrCl₂        (4,7-Me₂Ind=4,7-dimethylindenyl) activated with an alumoxane,        such as methylalumoxane or modified methylalumoxane;    -   (52) meso-CH₂CH₂(2-MeInd)₂ZrMe₂ and rac-CH₂CH₂(4,7-Me₂Ind)₂ZrMe₂        activated with a non-coordinating anion activator, such as        N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or        triphenylcarbonium tetrakis(pentaflourophenyl)boron;    -   (53) meso-Me₂Si(2-MeInd)₂ZrCl₂ and rac-CH₂CH₂(4,7-Me₂Ind)₂ZrCl₂        activated with an alumoxane, such as methylalumoxane or modified        methylalumoxane; and    -   (54) meso-Me₂Si(2-MeInd)₂ZrMe₂ and rac-CH₂CH₂(4,7-Me₂Ind)₂ZrMe₂        activated with a non-coordinating anion activator, such as        N,N-dimethylanilinium tetrakis(pentaflourophenyl)boron or        triphenylcarbonium tetrakis(pentaflourophenyl)boron.

The two transition metal compounds (pre-catalysts) may be used in anyratio. Preferred molar ratios of (A) transition metal compound toproduce amorphous polymer to (B) transition metal compound to producecrystalline polymer fall within the range of (A:E) 1:1000 to 1000: 1,alternatively 1:100 to 500:1, alternatively 1:10 to 200:1, alternatively1:1 to 100:1, and alternatively 1:1 to 75:1, and alternatively 5:1 to50:1. The particular ratio chosen will depend on the exact pre-catalystschosen, the method of activation, and the end product desired. In aparticular embodiment, when using the two pre-catalysts (A-“amorphouspolymer producing precatalyst” and B-“crystalline polymer producingcatalyst”), where both are activated with the same activator, thepreferred mole percents, based upon the molecular weight of thepre-catalysts, are 10 to 99.9% A to 0.1 to 90% B, alternatively 25 to99% A to 0.5 to 50% B, alternatively 50 to 99% A to 1 to 25% B, andalternatively 75 to 99% A to 1 to 10% B.

In general the combined pre-catalyst compounds and the activator arecombined in ratios of about 1:10,000 to about 10:1. When alumoxane oraluminum alkyl activators are used, the combinedpre-catalyst-to-activator molar ratio is from 1:5000 to 10:1,alternatively from 1:1000 to 10:1; alternatively, 1:500 to 2:1; or 1:300to 1:1. When ionizing activators are used, the combinedpre-catalyst-to-activator molar ratio is from 10:1 to 1:10; 5:1 to 1:5;2:1 to 1:2; or 1.2:1 to 1:1. Multiple activators may be used, includingusing mixes of alumoxanes or aluminum alkyls with ionizing activators.

In another preferred embodiment a third catalyst (pre-catalyst plusactivator) is present in the processes described above. The thirdcatalyst may be any of the pre-catalyst components listed herein.Preferred third pre-catalysts include those that are capable ofproducing waxes. Preferred examples include:rac-dimethylsilylbis(4,7-dimethylindenyl)hafnium dichloride,rac-dimethylsilylbis(4,7-dimethylindenyl)hafnium dimethyl,rac-dimethylsilylbis(4,7-dimethylindenyl)zirconium dichloride,rac-dimethylsilylbis(4,7-dimethylindenyl)zirconium dimethyl,rac-dimethylsilylbis(indenyl) hafnium dichloride,rac-dimethylsilylbis(indenyl)hafnium dimethyl,rac-dimethylsilylbis(indenyl)zirconium dichloride,rac-dimethylsilylbis(indenyl)zirconium dimethyl,rac-dimethylsilylbis(tetrahydroindenyl)hafnium dichloride,rac-dimethylsilylbis(tetrahydroindenyl)hafnium dimethyl,rac-dimethylsilylbis(tetrahydroindenyl)zirconium dichloride,rac-dimethylsilylbis(tetrahydroindenyl)zirconium dimethyl,rac-diphenylsilylbis(4,7-dimethylindenyl)hafnium dichloride,rac-diphenylsilylbis(4,7-dimethylindenyl)hafnium dimethyl,rac-diphenylsilylbis(4,7-dimethylindenyl)zirconium dichloride,rac-diphenylsilylbis(4,7-dimethylindenyl)zirconium dimethyl,rac-diphenylsilylbis(indenyl) hafnium dichloride,rac-diphenylsilylbis(indenyl)hafnium dimethyl,rac-diphenylsilylbis(indenyl)zirconium dichloride,rac-diphenylsilylbis(indenyl)zirconium dimethyl,rac-diphenylsilylbis(tetrahydroindenyl)hafnium dichloride,rac-diphenylsilylbis(tetrahydroindenyl)hafnium dimethyl,rac-diphenylsilylbis(tetrahydroindenyl)zirconium dichloride,rac-diphenylsilylbis(tetrahydroindenyl)zirconium dimethyl,rac-methylphenylsilylbis(4,7-dimethylindenyl)hafnium dichloride,rac-methylphenylsilylbis(4,7-dimethylindenyl)hafnium dimethyl,rac-methylphenylsilylbis(4,7-dimethylindenyl)zirconium dichloride,rac-methylphenylsilylbis(4,7-dimethylindenyl)zirconium dimethyl,rac-methylphenylsilylbis(indenyl)hafnium dichloride,rac-methylphenylsilylbis(indenyl)hafnium dimethyl,rac-methylphenylsilylbis(indenyl)zirconium dichloride,rac-methylphenylsilylbis(indenyl)zirconium dimethyl,rac-methylphenylsilylbis(tetrahydroindenyl)hafnium dichloride,rac-methylphenylsilylbis(tetrahydroindenyl)hafnium dimethyl,rac-methylphenylsilylbis(tetrahydroindenyl) zirconium dichloride,rac-methylphenylsilylbis(tetrahydroindenyl)zirconium dimethyl,rac-ethylenebis(4,7-dimethylindenyl)hafnium dichloride,rac-ethylenebis(4,7-dimethylindenyl)hafnium dimethyl,rac-ethylenebis(4,7-dimethylindenyl)zirconium dichloride,rac-ethylenebis(4,7-dimethylindenyl)zirconium dimethyl,rac-ethylenebis(indenyl)hafnium dichloride, rac-ethylenebis(indenyl)hafnium dimethyl, rac-ethylenebis(indenyl)zirconium dichloride,rac-ethylenebis(indenyl)zirconium dimethyl,rac-ethylenebis(tetrahydroindenyl)hafnium dichloride,rac-ethylenebis(tetrahydroindenyl)hafnium dimethyl,rac-ethylenebis(tetrahydroindenyl)zirconium dichloride, andrac-ethylenebis(tetrahydroindenyl)zirconium dimethyl

Three transition metal. compounds (pre-catalysts) may be used in anyratio. Preferred molar ratios of (A) transition metal compound toproduce amorphous polypropylene to (B) transition metal compound toproduce crystalline polypropylene to (C) transition metal compound toproduce wax fall within the range of (A:B:C) 1:1000:500 to 1000:1:1,alternatively 1:100:50 to 500:1:1, alternatively 1:10:10 to 200:1:1,alternatively 1:1:1 to 100:1:50, and alternatively 1:1:10 to 75:1:50,and alternatively 5:1:1 to 50:1:50. The particular ratio chosen willdepend on the exact pre-catalysts chosen, the method of activation, andthe end product desired.

Additional preferred catalysts and process are described in U.S. Pat.Nos. 6,376,410 and 6,380,122, which are incorporated by referenceherein.

In another embodiment the catalyst compositions of this inventioninclude a support material or carrier. For example, the one or morecatalyst components and/or one or more activators may be deposited on,contacted with, vaporized with, bonded to, or incorporated within,adsorbed or absorbed in, or on, one or more supports or carriers.

The support material is any of the conventional support materials.Preferably the supported material is a porous support material, forexample, talc, inorganic oxides and inorganic chlorides. Other supportmaterials include resinous support materials such as polystyrene,functionalized or crosslinked organic supports, such as polystyrenedivinyl benzene polyolefins or polymeric compounds, zeolites, clays, orany other organic or inorganic support material and the like, ormixtures thereof.

The preferred support materials are inorganic oxides that include thoseGroup 2, 3, 4, 5, 13 or 14 metal oxides. The preferred supports includesilica, which may or may not be dehydrated, fumed silica, alumina (WO99/60033), silica-alumina and mixtures thereof. Other useful supportsinclude magnesia, titania, zirconia, magnesium chloride (U.S. Pat. No.5,965,477), montmorillonite (European Patent EP-B1 0 511 665),phyllosilicate, zeolites, talc, clays (U.S. Pat. No. 6,034,187) and thelike. Also, combinations of these support materials may be used, forexample, silica-chromium, silica-alumina, silica-titania and the like.Additional support materials may include those porous acrylic polymersdescribed in EP 0 767 184 B1, which is incorporated herein by reference.Other support materials include nanocomposites as described in PCT WO99/47598, aerogels as described in WO 99/48605, spherulites as describedin U.S. Pat. No. 5,972,510 and polymeric beads as described in WO99/50311, which are all herein incorporated by reference.

It is preferred that the support material, most preferably an inorganicoxide, has a surface area in the range of from about 10 to about 700m²/g, pore volume in the range of from about 0.1 to about 4.0 cc/g andaverage particle size in the range of from about 5 to about 500 μm. Morepreferably, the surface area of the support material is in the range offrom about 50 to about 500 m²/g, pore volume of from about 0.5 to about3.5 cc/g and average particle size of from about 10 to about 200 μm.Most preferably the surface area of the support material is in the rangeis from about 100 to about 400 m²/g, pore volume from about 0.8 to about3.0 cc/g and average particle size is from about 5 to about 100 μm. Theaverage pore size of the carrier useful in the invention typically haspore size in the range of from 10 to 1000 Å, preferably 50 to about 500Å, and most preferably 75 to about 350 Å.

As is well known in the art, the catalysts may also be supportedtogether on one inert support, or the catalysts may be independentlyplaced on two inert supports and subsequently mixed. Of the two methods,the former is preferred.

In another embodiment the support may comprise one or more types ofsupport material which may be treated differently. For example one coulduse tow different silicas that had different pore volumes or had beencalcined at different temperatures. Likewise one, could use a silicathat had been treated with a scavenger or other additive and a silicathat had not.

The stereospecific catalysts may be used to prepare macromonomer havinga Mw of 100,000 or less and a crystallinity of 30% or more preferablyhaving vinyl termini.

As a specific example, a method for preparing propylene-basedmacromonomers having a high percentage of vinyl terminal bonds involves:

-   -   a) contacting, in solution, propylene, optionally a minor amount        of copolymerizable monomer, with a catalyst composition        containing the stereorigid, activated transition metal catalyst        compound at a temperature from about 80° C. to about 140° C.;        and    -   b) recovering isotactic or syndiotactic polypropylene chains        having number average molecular weights of about 2,000 to about        30,000 Daltons.

Preferably, the solution comprises a hydrocarbon solvent. Morepreferably, the hydrocarbon solvent is aliphatic or aromatic. Also, thepropylene monomers are preferably contacted at a temperature from 90° C.to 120° C. More preferably, a temperature from 95° C. to 115° C. isused. Most preferably, the propylene monomers are contacted at atemperature from 100° C. to 110° C. Reactor pressure generally can varyfrom atmospheric to 345 MPa, preferably to 182 MPa. The reactions can berun in batch or in continuous mode. Conditions for suitable slurry-typereactions will also be suitable and are similar to solution conditions,the polymerization typically being run in liquid propylene underpressures suitable to such.

The catalyst pair selection criteria were discussed earlier. Onecatalyst typically is stereospecific with the ability to producesignificant population of vinyl-terminated macromonomers, the othertypically is a specific and capable of incorporating the reactivemacromonomers. In general it is believed that C2 symmetric bulky ligandmetallocene catalysts can produce vinyl terminated isotacticpolypropylene macromonomers. Catalysts that favor betamethyl-eliminationalso often appear to also favor isotactic polypropylene macromonomerformation. Rac-dimethylsilyl bis(indenyl)hafnium dimethyl, dimethylsilylbis(2-methyl-4-phenylindenyl) zirconium dlichloride, and rac-ethylenebis(4,7-dimethylindenyl) hafnium dimethyl are catalysts capable ofproducing isotactic polypropylene having high vinyl chain terminationfor use in this invention. High temperatures, typically above 80° C.,appear to positively influence vinyl termination. Likewise,Me₂Si(Me₄C₅)(N-c-Cl₂H₂₃)TiMe₂ and Me₂Si(Me₄C₅)(N-c-C₁₂H₂₃)TiMe₂ produceamorphous polypropylene useful in this invention and are believed toincorporate the vinyl terminated macromonomers to also produce a graftedstructure of scPP side chains on an amorphous backbone.

In alternate embodiments dienes such as 1,9-decadiene are introducedinto the reaction zone to promote the production of vinyl-terminated aPPand scPP macromonomers that help increase the population of branch-blockspecies.

Polymerization Processes

The catalysts and catalyst systems described above are suitable for usein a solution, bulk, gas or slurry polymerization process or acombination thereof, preferably solution phase or bulk phasepolymerization process. [00230] In one embodiment, this invention isdirected toward the solution, bulk, slurry or gas phase polymerizationreactions involving the polymerization of one or more of monomers havingfrom 3 to 30 carbon atoms, preferably 3-12 carbon atoms, and morepreferably 3 to 8 carbon atoms. Preferred monomers include one or moreof propylene, butene-1, pentene-1,4-methyl-pentene-1, hexene-1,octene-1, decene-1,3-methyl-pentene-1, and cyclic olefins or acombination thereof. Other monomers can include vinyl monomers,diolefins such as dienes, polyenes, norbornene, norbornadiene, vinylnorbornene, ethylidene norbornene monomers. Preferably a homopolymer orcopolymer of propylene is produced. In another embodiment, both ahomopolymer of propylene and a copolymer of propylene and one or more ofthe monomers listed above are produced.

One or more reactors in series or in parallel may be used in the presentinvention. Catalyst component and activator may be delivered as asolution or slurry, either separately to the reactor, activated in-linejust prior to the reactor, or preactivated and pumped as an activatedsolution or slurry to the reactor. A preferred operation is twosolutions activated in-line. For more information on methods tointroduce multiple catalysts into reactors, please see U.S. Pat. No.6,399,722, and WO0130862A1. While these references may emphasize gasphase reactors, the techniques described are equally applicable to othertypes of reactors, including continuous stirred tank reactors, slurryloop reactors and the like. Polymerizations are carried out in eithersingle reactor operation, in which monomer, comonomers,catalyst/activator, scavenger, and optional modifiers are addedcontinuously to a single reactor or in series reactor operation, inwhich the above components are added to each of two or more reactorsconnected in series. The catalyst components can be added to the firstreactor in the series. The catalyst component may also be added to bothreactors, with one component being added to first reaction and anothercomponent to other reactors.

In one embodiment 500 ppm or less of hydrogen is added to thepolymerization, or 400 ppm or less, or 300 ppm or less. In otherembodiments at least 50 ppm of hydrogen is added to the polymerization,or 100 ppm or more, or 150 ppm or more.

Gas Phase Polymerization

Generally, in a fluidized gas bed process used for producing polymers, agaseous stream containing one or more monomers is continuously cycledthrough a fluidized bed in the presence of a catalyst under reactiveconditions. The gaseous stream is withdrawn from the fluidized bed andrecycled back into the reactor. Simultaneously, polymer product iswithdrawn from the reactor and fresh monomer is added to replace thepolymerized monomer. (See for example U.S. Pat. Nos. 4,543,399,4,588,790, 5,028,670, 5,317,036, 5,352,749, 5,405,922, 5,436,304,5,453,471, 5,462,999, 5,616,661 and 5,668,228 all of which are fullyincorporated herein by reference.)

Slurry Phase Polymerization

A slurry polymerization process generally operates between 1 to about 50atmosphere pressure range (15 psi to 735 psi, 103 kPa to 5068 kPa) oreven greater and temperatures in the range of 0° C. to about 120° C. Ina slurry polymerization, a suspension of solid, particulate polymer isformed in a liquid polymerization diluent medium to which monomer andcomonomers along with catalyst are added. The suspension includingdiluent is intermittently or continuously removed from the reactor wherethe volatile components are separated from the polymer and recycled,optionally after a distillation, to the reactor. The liquid diluentemployed in the polymerization medium is typically an alkane having from3 to 7 carbon atoms, preferably a branched alkane. The medium employedshould be liquid under the conditions of polymerization and relativelyinert. When a propane medium is used the process must be operated abovethe reaction diluent critical temperature and pressure. Preferably, ahexane or an isobutane medium is employed.

In one embodiment, a preferred polymerization technique useful in theinvention is referred to as a particle form polymerization, or a slurryprocess where the temperature is kept below the temperature at which thepolymer goes into solution. Such technique is well known in the art, anddescribed in for instance U.S. Pat. No. 3,248,179 which is fullyincorporated herein by reference. The preferred temperature in theparticle form process is within the range of about 85° C. to about 110°C. Two preferred polymerization methods for the slurry process are thoseemploying a loop reactor and those utilizing a plurality of stirredreactors in series, parallel, or combinations thereof. Non-limitingexamples of slurry processes include continuous loop or stirred tankprocesses. Also, other examples of slurry processes are described inU.S. Pat. No. 4,613,484, which is herein fully incorporated byreference.

In another embodiment, the slurry process is carried out continuously ina loop reactor. The (catalyst, as a slurry in isobutane or as a dry freeflowing powder, is injected regularly to the reactor loop, which isitself filled with circulating slurry of growing polymer particles in adiluent of isobutane containing monomer and comonomer. Hydrogen,optionally, may be added as a molecular weight control. (In oneembodiment 500 ppm or less of hydrogen is added, or 400 ppm or less or300 ppm or less. In other embodiments at least 50 ppm of hydrogen isadded, or 100 ppm or more, or 150 ppm or more.)

The reactor is maintained at a pressure of 3620 kPa to 4309 kPa and at atemperature in the range of about 60° C. to about 104° C. depending onthe desired polymer melting characteristics. Reaction heat is removedthrough the loop wall since much of the reactor is in the form of adouble-jacketed pipe. The slurry is allowed to exit the reactor atregular intervals or continuously to a heated low pressure flash vessel,rotary dryer and a nitrogen purge column in sequence for removal of theisobutane diluent and all unreacted monomer and comonomers. Theresulting hydrocarbon free powder is then compounded for use in variousapplications.

In another embodiment, the reactor used in the slurry process useful inthe invention is capable of and the process useful in the invention isproducing greater than 2000 lbs. of polymer per hour (907 Kg/hr), morepreferably greater than 5000 lbs./hr (2268 Kg/hr), and most preferablygreater than 10,000 lbs./hr (4540 Kg/hr). In another embodiment theslurry reactor used in the process useful in the invention is producinggreater than 15,000 lbs. of polymer per hour (6804 Kg/hr), preferablygreater than 25,000 lbs./hr (11,340 Kg/hr) to about 100,000 lbs./hr(45,500 Kg/hr).

In another embodiment in the slurry process useful in the invention thetotal reactor pressure is in the range of from 400 psig (2758 kPa) to800 psig (5516 kPa), preferably 450 psig (3103 kPa) to about 700 psig(4827 kPa), more preferably 500 psig (3448 kPa) to about 650 psig (4482kPa), most preferably from about 525 psig (3620 kPa) to 625 psig (4309kPa).

In yet another embodiment in the slurry process useful in the inventionthe concentration of predominant monomer in the reactor liquid medium isin the range of from about 1 to 10 weight percent, preferably from about2 to about 7 weight percent, more preferably from about 2.5 to about 6weight percent, most preferably from about 3 to about 6 weight percent.

Another process useful in the invention is where the process, preferablya slurry process is operated in the absence of or essentially free ofany scavengers, such as triethylaluminum, trimethylaluminum,tri-isobutylaluminum and tri-n-hexylaluminum and diethyl aluminumchloride, dibutyl zinc and the like. This process is described in PCTpublication WO 96/08520 and U.S. Pat. No. 5,712,352, which are hereinfully incorporated by reference.

In another embodiment the process is run with scavengers. Typicalscavengers include trimethyl aluminum, tri-isobutyl aluminum and anexcess of alumoxane or modified alumoxane.

Homogeneous, Bulk, or Solution Phase Polymerization

The catalysts described herein can be used advantageously in homogeneoussolution processes. Generally this involves polymerization in acontinuous reactor in which the polymer formed and the starting monomerand catalyst materials supplied, are agitated to reduce or avoidconcentration gradients. Suitable processes operate above the meltingpoint of the polymers at high pressures, from 1 to 3000 bar (10-30,000MPa), in which the monomer acts as diluent or in solution polymerizationusing a solvent.

Temperature control in the reactor is obtained by balancing the heat ofpolymerization with reactor cooling by reactor jackets or cooling coilsto cool the contents of the reactor, auto refrigeration, pre-chilledfeeds, vaporization of liquid medium (diluent, monomers or solvent) orcombinations of all three. Adiabatic reactors with pre-chilled feeds mayalso be used. The reactor temperature depends on the catalyst used. Ingeneral, the reactor temperature preferably can vary between about 30°C. and about 160° C., more preferably from about 90° C. to about 150°C., and most preferably from about 100° C. to about 140° C.Polymerization temperature may vary depending on catalyst choice. Forexample a diimine Ni catalyst may be used at 40° C., while a metalloceneTi catalyst can be used at 100° C. or more. In series operation, thesecond reactor temperature is preferably higher than the first reactortemperature. In parallel reactor operation, the temperatures of the tworeactors are independent. The pressure can vary from about 1 mm Hg to2500 bar (25,000 MPa), preferably from 0.1 bar to 1600 bar (1-16,000MPa), most preferably from 1.0 to 500 bar (10-5000 MPa).

In one embodiment 500 ppm or less of hydrogen is added to thepolymerization, or 400 ppm or less or 300 ppm or less. In otherembodiments at least 50 ppm of hydrogen is added t) the polymerization,or 100 ppm or more, or 150 ppm or more.

Each of these processes may also be employed in single reactor, parallelor series reactor configurations. The liquid processes comprisecontacting olefin monomers with the above described catalyst system in asuitable diluent or solvent and allowing said monomers to react for asufficient time to produce the desired polymers. Hydrocarbon solventsare suitable, both aliphatic and aromatic. Alkanes, such as hexane,pentane, isopentane, and octane, are preferred.

The process can be carried out in a continuous stirred tank reactor,batch reactor or plug flow reactor, or more than one reactor operated inseries or parallel. These reactors may have or may not have internalcooling or heating and the monomer feed may or may not be refrigerated.See the general disclosure of U.S. Pat. No. 5,001,205 for generalprocess conditions. See also, international application WO 96/33227 andWO 97/22639. All documents are incorporated by reference for US purposesfor description of polymerization processes, metallocene selection anduseful scavenging compounds.

This invention further relates to a continuous process to prepare anadhesive comprising:

-   -   1) combining monomer, optional solvent, catalyst and activator        in a reactor system,    -   2) withdrawing polymer solution from the reactor system,    -   3) removing at least 100/6 solvent, if present, from the polymer        solution,    -   4) quenching the reaction,    -   5) devolatilizing the polymer solution to form molten polymer,    -   6) combining the molten polymer and one or more additives (such        as those described below) in a mixer, such as a static mixer,(in        a preferred embodiment tackifier is not added or is added in        amounts of less than 30 weight %, preferably less than 20 weight        %, more preferably in amounts of less than 10 weight %),    -   7) removing the polymer combination from the mixer, and    -   8) pelletizing or drumming the polymer combination; where        step 1) comprises any of the processes described above.

In another embodiment this invention relates to a continuous process toprepare an adhesive comprising:

-   -   1) combining monomer, optional solvent, catalyst and activator        in a reactor system,    -   2) withdrawing polymer solution from the reactor system,    -   3) removing at least 10% solvent, if present, from the polymer        solution,    -   4) quenching the reaction,    -   5) devolatilizing the polymer solution to form molten polymer,    -   6) combining the molten polymer and one or more additives in a        mixer, such as a static mixer,    -   7) removing the polymer combination from the mixer, and    -   8) pelletizing or drumming the polymer combination.

In a particularly preferred embodiment, this invention relates to acontinuous process to make an adhesive comprising

-   -   1) selecting a first catalyst component capable of producing a        polymer having an Mw of 100,000 or less and a crystallinity of        20% or less under selected polymerization conditions;    -   2) selecting a second catalyst component capable of producing        polymer having an Mw of 100,000 or less and a crystallinity of        40% or more at the selected polymerization conditions;    -   3) contacting, in a solvent and in a reaction zone under the        selected polymerization conditions, the catalyst components in        the presence of one or more activators with one or more C3 to        C40 olefins, and, optionally one or more diolefins;    -   4) at a temperature of greater than 100° C.;    -   5) at a residence time of 120 minutes or less (preferably 60 to        120 minutes);    -   6) wherein the ratio of the first catalyst to the second        catalyst is from 1:1 to 50:1;    -   7) wherein the activity of the catalyst components is at least        50 kilograms of polymer per gram of the catalyst components; and        wherein at least 20% of the olefins are converted to polymer;    -   8) withdrawing polymer solution from the reaction zone;    -   9) removing at least 100/,% solvent from the polymer solution;    -   10) quenching the reaction;    -   11) devolatilizing the polymer solution to form molten polymer;    -   12) combining the molten polymer and one or more additives in a        mixer, such as a static mixer;    -   13) removing the polymer combination from the mixer; and    -   14) pelletizing or drumming the polymer combination.

In a particularly preferred embodiment, this invention relates to acontinuous process to make an adhesive comprising

-   -   1) selecting a first catalyst component capable of producing a        polymer having an Mw of 100,000 or less and a crystallinity of        20% or less under selected polymerization conditions;    -   2) selecting a second catalyst component capable of producing        polymer having an Mw of 100,000 or less and a crystallinity of        40% or more at the selected polymerization conditions;    -   3) contacting, in a solvent and in a reaction zone under the        selected polymerization conditions, the catalyst components in        the presence of one or more activators with one or more C3 to        C40 olefins, and, optionally one or more diolefins;    -   4) at a temperature of greater than 100° C.;    -   5) at a residence time of 120 minutes or less;    -   6) wherein the ratio of the first catalyst to the second        catalyst is from 1:1 to 50:1;    -   7) wherein the activity of the catalyst components is at least        50 kilograms of polymer per gram of the catalyst components; and        wherein at least 50% of the olefins are converted to polymer;    -   8) withdrawing polymer solution from the reaction zone;    -   9) removing at least 10% solvent from the polymer solution;    -   10) quenching the reactiorn;    -   11) forming molten polymer        -   where the polymer comprises one or more C3 to C40 olefins,            and less than 50 mole % of ethylene, and where the polymer            has:        -   a) a Dot T-Peel of 1 Newton or more; and        -   b) a branching index (g′) of 0.95 or less measured at the Mz            of the polymer; and        -   c) an Mw of 100,000 or less; and    -   12) combining the molten polymer and one or more additives in a        mixer, such as a static mixer;    -   13) removing the polymer combination from the mixer; and    -   14) pelletizing or drumming the polymer combination.

In a particularly preferred embodiment, this invention relates to acontinuous process to make an adhesive comprising

-   -   1) selecting a first catalyst component capable of producing a        polymer having an Mw of 100.,000 or less and a crystallinity of        20% or less under selected polymerization conditions;    -   2) selecting a second catalyst component capable of producing        polymer having an Mw of 100,000 or less and a crystallinity of        40% or more at the selected polymerization conditions;    -   3) contacting, in a solvent and in a reaction zone under the        selected polymerization conditions, the catalyst components in        the presence of one or more activators with one or more C3 to        C40 olefins, and, optionally one or more diolefins;    -   4) at a temperature of greater than 100° C.;    -   5) at a residence time of 120 minutes or less;    -   6) wherein the ratio of the first catalyst to the second        catalyst is from 1:1 to 50:1;    -   7) wherein the activity of the catalyst components is at least        50 kilograms of polymer per gram of the catalyst components; and        wherein at least 50% of the olefins are converted to polymer;    -   8) withdrawing polymer solution from the reaction zone;    -   9) removing at least 10% solvent from the polymer solution;    -   10) quenching the reaction;    -   11) forming molten polymer        -   where the polymer comprises one or more C3 to C40 olefins            (preferably propylene), and less than 50 mole % of ethylene,            and where the polymer has:        -   a) a Dot T-Peel of 3 Newton or more; and        -   b) a branching index (g′) of 0.90 or less measured at the Mz            of the polymer; and        -   c) an Mw of 30,000 or less;        -   d) a peak melting,, point between 60 and 190° C.,        -   e) a Heat of fusion of 1 to 70 J/g,        -   f) a melt viscosity of 8000 mPa·sec or less at 190° C.; and    -   12) combining the molten polymer and one or more additives in a        mixer, such as a static mixer;    -   13) removing the polymer combination from the mixer; and    -   14) pelletizing or drumming the polymer combination.

In another embodiment this invention relates to a continuous process toprepare an adhesive comprising:

-   -   1) combining monomer, catalyst and activator in a reactor        system,    -   2) withdrawing polymer from the reactor system,    -   3) quenching the reaction,    -   4) forming molten polymer,    -   5) combining the molten. polymer and one or more additives, and    -   6) pelletizing or drumming the polymer combination.        Formulations of the Polymers

The polymers produced herein then can be used directly as an adhesive orblended with other components to form an adhesive.

Tackifiers are typically not needed with the polymers of this invention.However if tackifier is de-sired, the tackifiers that may be blendedwith the polymers described above are those typically used in the art.Examples include, but are not limited to, aliphatic hydrocarbon resins,aromatic modified aliphatic hydrocarbon resins, hydrogenatedpolycyclopentadiene resins, polycyclopentadiene resins, gum rosins, gumrosin esters, wood rosins, wood rosin esters, tall oil rosins, tall oilrosin esters, polyterpenes, aromatic modified polyterpenes, terpenephenolics, aromatic modified hydrogenated polycyclopentadiene resins,hydrogenated aliphatic resin, hydrogenated aliphatic aromatic resins,hydrogenated terpenes and modified terpenes, and hydrogenated rosinesters. In some embodiments the tackifier is hydrogenated. In otherembodiments the tackifier is non-polar. (Non-polar meaning that thetackifier is substantially free of monomers having polar groups.Preferably the polar groups are not present, however if they arepreferably they are not present at more that 5 weight %, preferably notmore that 2 weight %, even more preferably no more than 0.5 weight %.)In some embodiments the tackifier has a softening point (Ring and Ball,as measured by ASTM E-28) of 80° C. to 150° C., preferably 100° C. to130° C.

The tackifier, if present, is typically present at about 1 weight % toabout 80 weight %, based upon the weight of the blend, more preferably 2weight % to 40 weight %, even more preferably 3 weight % to 30 weight %.

Preferred hydrocarbon resins for use as tackifiers or modifiers include:

-   1. Resins such as C5/C6 terpene resins, styrene terpenes,    alpha-methyl styrene terpene resins, C9 terpene resins, aromatic    modified C5/C6, aromatic modified cyclic resins, aromatic modified    dicyclopentadiene based resins or mixtures thereof Additional    preferred resins include those described in WO 91/07472, U.S. Pat.    No. 5,571,867, U.S. Pat. No. 5,171,793 and U.S. Pat. No. 4,078,132.    Typically these resins are obtained from the cationic polymerization    of compositions containing one or more of the following monomers: C5    diolefins (such1 as 1-3 pentadiene, isoprene, etc); C5 olefins (such    as 2-methylbutenes, cyclopentene, etc.); C6 olefins (such as    hexene), C9 vinylaromatics (such as styrene, alpha methyl styrene,    vinyltoluene, indene, methyl indene, etc.); cyclics (such as    dicyclopentadiene, methyldicyclopentadiene, etc.); and or terpenes    (such as limonene, carene, etc).-   2. Resins obtained by the thermal polymerization of    dicyclopentadiene, and/or the thermal polymerization of dimers or    oligomers of cyclopentadiene and/or methylcyclopentadiene,    optionally with vinylaromatics (such as styrene, alpha-methyl    styrene, vinyl toluene, indene, methyl indene).

The resins obtained after polymerization and separation of unreactedmaterials, can be hydrogenated if desired. Examples of preferred resinsinclude those described in U.S. Pat. No. 4,078,132; WO 91/07472; U.S.Pat. No. 4,994,516; EP 0 046 344 A; EP 0 082 726 A; and U.S. Pat. No.5,171,793.

In another embodiment an adhesive composition comprising polymer productof this invention further comprises a crosslinking agent. Preferredcrosslinking agents include those having functional groups that canreact with the acid or anhydride group. Preferred crosslinking agentsinclude alcohols, multiols, amines, diamines and/or triamines. Examplesof crosslinking agents useful in this invention include polyamines suchas ethylenediamine, diethylenetriamine, hexamethylenediamine,diethylaniinopropylamine, and/or menthanediamine.

In another embodiment an adhesive composition comprising the polymerproduct of this invention further comprises typical additives known inthe art such as fillers, antioxidants, adjuvants, adhesion promoters,oils, and/or plasticizers. Preferred fillers include titanium dioxide,calcium carbonate, barium sulfate, silica, silicon dioxide, carbonblack, sand, glass beads, mineral aggregates, talc, clay and the like.Preferred antioxidants include phenolic antioxidants, such as Irganox1010, Irganox, 1076 both available from Ciba-Geigy. Preferred oilsinclude paraffinic or napthenic oils such as Primol 3 52, or Primol 876available from ExxonMobil Chemical France, S.A. in Paris, France.Preferred plasticizers include polybutenes, such as Parapol 950 andParapol 1300 available from ExxonMobil Chemical Company in HoustonTexas. Other preferred additives include block, antiblock, pigments,processing aids, UV stabilizers, neutralizers, lubricants, surfactantsand/or nucleating agents may also be present in one or more than onelayer in the films. Preferred additives include silicon dioxide,titanium dioxide, polydimethylsiloxane, talc, dyes, wax, calciumsterate, carbon black, low molecular weight resins and glass beads.Preferred adhesion promoters include polar acids, polyaminoamides (suchas Versamid 115, 125, 140, available from Henkel), urethanes (such asisocyanate/hydroxy terminated polyester systems, e.g. bonding agentTN/Mondur Cb-75(Miles, Inc.), coupling agents, (such as silane esters(Z-6020 from Dow Coming)), titanate esters (such as Kr-44 available fromKenrich), reactive acrylate monomers (such as sarbox SB-600 fromSartomer), metal acid salts (such as Saret 633 from Sartomer),polyphenylene oxide, oxidized polyolefins, acid modified polyolefins,and anhydride modified polyolefins.

In another embodiment the polymers of this invention are combined withless than 3 wt % anti--oxidant, less than 3 wt % flow improver, lessthan 10 wt % wax, and or less than 3 wt % crystallization aid.

Other optional components that may be combined with the polymer productof this invention are plasticizers or other additives such as oils,surfactants, fillers, color masterbatches, and the like. Preferredplasticizers include mineral oils, polybutenes, phthalates and the like.Particularly preferred plasticizers include phthalates such asdiisoundecyl phthalate (DIUP), diisononylphthalate (DINP),dioctylphthalates (DOP) and the like. Particularly preferred oilsinclude aliphatic naphthenic oils.

Other optional components that may be combined with the polymer productof this invention are low molecular weight products such as wax, oil orlow Mn polymer, (low meaning below Mn of 5000, preferably below 4000,more preferably below 3000, even more preferably below 2500). Preferredwaxes include polar or non-polar waxes, functionalized waxes,polypropylene waxes, polyethylene waxes, and wax modifiers. Preferredwaxes include ESCOMER™ 101. Preferred functionalized waxes include thosemodified with an alcohol, an acid, a ketone, an anhydride and the like.Preferred examples include waxes modified by methyl ketone, maleicanhydride or maleic acid. Preferred oils include aliphatic napthenicoils, white oils or the like. Preferred low Mn polymers include polymersof lower alpha olefins such as propylene, butene, pentene, hexene andthe like. A particularly preferred polymer includes polybutene having anMn of less than 1000. An example of such a polymer is available underthe trade name PARAPOL™ 950 from ExxonMobil Chemical Company. PARAPOL™950 is a liquid polybutene polymer having an Mn of 950 and a kinematicviscosity of 220cSt at 100° C., as measured by ASTM D 445. In someembodiments the polar and non-polar waxes are used together in the samecomposition.

In some embodiments, however, wax may not be desired and is present atless than 5 weight % , preferably less than 3 weight %, more preferablyless than 1 weight %, more preferably less than 0.5 weight %, based uponthe weight of the composition.

In another embodiment the polymers of this invention have less than 30weight % total of any combination of additives described above,preferably less than 25 weight %, preferably less, than 20 weight %,preferably less than 15 weight %, preferably less than 10 weight %,preferably less than 5 weight %, based upon the weight of the polymerand the additives.

In another embodiment the polymer produced by this invention may beblended with elastomers (preferred elastomers include all natural andsynthetic rubbers, including those defined in ASTM D1566). In apreferred embodiment elastomers are blended with the polymer produced bythis invention to form rubber toughened compositions. In a particularlypreferred embodiment the rubber toughened composition is a two (or more)phase system where the rubber is a discontinuous phase and the polymeris a continuous phase. Examples of preferred elastomers include one ormore of the following: ethylene propylene rubber, ethylene propylenediene monomer rubber, neoprene rubber, styrenic block copolymer rubbers(including SI, SIS, SB, SBS, SIBS and the like), butyl rubber, halobutylrubber, copolymers of isobutylene and para-alkylstyrene, halogenatedcopolymers of isobutylene and para-alkylstyrene. This blend may becombined with the tackifiers and/or other additives as described above.

In another embodiment the polymer produced by this invention may beblended with impact copolymers. Impact copolymers are defined to be ablend of isotactic PP and an elastomer such as an ethylene-propylenerubber. In a preferred embodiment the blend is a two (or more) phasesystem where the impact copolymer is a discontinuous phase and thepolymer is a continuous phase.

In another embodiment the polymer produced by this invention may beblended with ester polymers. In a preferred embodiment the blend is atwo (or more) phase system where the polyester is a discontinuous phaseand the polymer is a continuous phase.

In a preferred embodiment the polymers of the invention described aboveare combined with metallocene polyethylenes (mPE's) or metallocenepolypropylenes (mPP's). The mPE and mPP homopolymers or copolymers aretypically produced using mono- or bis-cyclopentadienyl transition metalcatalysts in combination with an activator of alumoxane and/or anon-coordinating anion in solution, slurry, high pressure or gas phase.The catalyst and activator may be supported or unsupported and thecyclopentadienyl rings by may substituted or unsubstituted. Severalcommercial products produced with such catalyst/activator combinationsare commercially available from ExxonMobil Chemical Company in Baytown,Tex. under the tradenaraes EXCEED™, ACHIEVE™ and EXACT™. For moreinformation on the methods and catalysts/activators to produce such ntPEhomopolymers and. copolymers see WO 94/26816; WO 94/03506; EPA 277,003;EPA 277,004; U.S. Pat. No. 5,153,157; U.S. Pat. No. 5,198,401; U.S. Pat.No. 5,240,894; U.S. Pat. No. 5,017,714; CA 1,268,753; U.S. Pat. No.5,324,800; EPA 129,368; U.S. Pat. No. 5,264,405; EPA 520,732; WO 9200333; U.S. Pat. No. 5,096,867; U.S. Pat. No. 5,507,475; EPA 426 637;EPA 573 403; EPA 520 732; EPA 495 375; EP3A 500 944; EPA 570 982;W091/09882; W094/03506 and U.S. Pat. No. 5,055,438.

In another embodiment the olefin polymer of this invention, preferablythe polypropylene homopolymer or copolymer of this invention, can beblended with another homopolymer and/or copolymer, including but notlimited to, homopolypropylene, propylene copolymerized with up to 50weight % of ethylene or a C4 to C20 alpha-olefin, isotacticpolypropylene, highly isotactic polypropylene, syndiotacticpolypropylene, random copolymer of propylene and ethylene and/or buteneand/or hexene, polybutene, ethylene vinyl acetate, low densitypolyethylene (density 0.915 to less than 0.935 g/cm³) linear low densitypolyethylene, ultra low density polyethylene (density 0.86 to less than0.90 g/cm³), very low density polyethylene (density 0.90 to less than0.915 g/cm³), medium density polyethylene (density 0.935 to less than0.945 g/cm³), high density polyethylene (density 0.945 to 0.98 g/cm³),ethylene vinyl acetate, ethylene methyl acrylate, copolymers of acrylicacid, polymethylmethacrylate or any other polymers polymerizable by ahigh-pressure free radical process, polyvinylchloride, polybutene-1,isotactic polybutene, ABS resins, elastomers such as ethylene-propylenerubber (EPR), vulcanized EPR, EPDM, block copolymer elastomers such asSBS, nylons (polyamides), polycarbonates, PET resins, crosslinkedpolyethylene, copolymers of ethylene and vinyl alcohol (EVOH), polymersof aromatic monomers such as polystyrene, poly-1 esters, high molecularweight polyethylene having a density of 0.94 to 0.98 g/cm³ low molecularweight polyethylene having a density of 0.94 to 0.98 g/cm³, graftcopolymers generally, polyacrylonitrile homopolymer or copolymers,thermoplastic polyamides, polyacetal, polyvinylidine fluoride and otherfluorinated elastomers, polyethylene glycols and polyisobutylene.

In a preferred embodiment the olefin polymer of this invention,preferably the polypropylene polymer of this invention, is present inthe blend at from 10 to 99 weight %, based upon the weight of thepolymers in the blend, preferably 20 to 95 weight %, even morepreferably at least 30 to 90 weight %, even more preferably at least 40to 90 weight %, even more preferably at least 50 to 90 weight %, evenmore preferably at least 60 to 90 weight %, even more preferably atleast 70 to 90 weight %.

The blends described above may be produced by mixing the two or morepolymers together, by connecting reactors together in series to makereactor blends or by using more than one cattlyst in the same reactor toproduce multiple species of polymer. The polymers cart be mixed togetherprior to being put into the extruder or may be mixed in an extruder. Anyof the above polymers, including the polymers produced by thisinvention, may be functionalized. Preferred functional groups includemaleic acid and maleic anhydride. By functionalized is meant that thepolymer has been contacted with an unsaturated acid or anhydride.Preferred unsaturated acids or anhydrides include any unsaturatedorganic compound containing at least one double bond and at least onecarbonyl group. Representative acids include carboxylic acids,anhydrides, esters and their salts, both metallic and non-metallic.Preferably the organic compound contains an ethylenic unsaturationconjugated with a carbonyl group (—C═O). Examples include maleic,fumaric, acrylic, methacrylic, itaconic, crotonic, alpha.methylcrotonic, and cinnamic acids as well as their anhydrides, esters andsalt derivatives. Maleic anhydride is particularly preferred. Theunsaturated acid or anhydride is preferably present at about 0.1 weight% to about 10 weight %, preferably at about 0.5 weight % to about 7weight %, even more preferably at about 1 to about 4 weight %, basedupon the weight of the hydrocarbon resin and the unsaturated acid oranhydride.

In a preferred embodiment the unsaturated acid or anhydried comprises acarboxylic acid or a derivative thereof selected from the groupconsisting of unsaturated carboxylic acids, unsaturated carboxylic acidderivatives selected from esters, imides, amides, anhydrides and cyclicacid anhydrides or mixtures thereof.

Applications

For purposes of this invention and the claims thereto, the followingtests are used, unless otherwise indicated.

Tensile strength, Tensile strength at break and elongation at break aremeasured by ASTM D 1708. Elongation at break is also called strain atbreak or percent elongation.

Peel strength-ASTM D-1876 (also referred to as Peel adhesion at 180°peel angle, 180° peel strength, 180° peel adhesion, T-Peel strength,T-Peel.)

Dynamic Storage modulus also called storage modulus is G′.

Creep resistance ASTM D-2293

Rolling Ball Tack PSTC 6

Hot Shear Strength is determined by suspending a 1000 gram weight from a25 mm wide strip of MYLAR polyester film coated with the polymer oradhesive formulation which is adhered to a stainless steel plate with acontact area of 12.5 mm×25 mm. The sample is placed in a ventilated ovenat 40° C. time is recorded until stress failure occurs.

Probe tack (also called Polyken probe tack) ASTM D 2979

Holding Power—PSTC 7 , also called Shear adhesion or Shear strength?.

Density—ASTM D792 at 25° C.

Gardner color ASTM D 1544-68.

SAFT is also called heat resistance.

Tensile Strength Modulus at 100% elongation and Young's Modulus aredetermined according to ASTM E-1876.

Luminence is the reflectance “Y” in the CIE color coordinates asdetermined by ASTM D 1925 divided by 100.

The polymer product of this invention or formulations thereof may thenbe applied directly to a substrate or may be sprayed thereon, typicallythe polymer is molten. Spraying is defined to include atomizing, such asproducing an even dot pattern, spiral spraying such as NordsonControlled Fiberization or oscillating a stretched filament like is donein the ITW Dynafiber/Omega heads or Summit technology from Nordson, aswell as melt blown techniques. Melt blown techniques are defined toinclude the methods described in U.S. Pat. No. 5,145,689 or any processwhere air streams are used to break up filaments of the extrudate andthen used to deposit the broken filaments on a substrate. In general,melt blown techniques are processes that use air to spin hot meltadhesive fibers and convey them onto a substrate for bonding. Fiberssizes can easily be controlled from 20-200 microns by changing the meltto air ratio. Few, preferably no, stray fibers are generated due to theinherent stability of adhesive melt blown applicators. Under UV lightthe bonding appears as a regular, smooth, stretched dot pattern.Atomization is a process that uses air to atomize hot melt adhesive intovery small dots and convey them onto a substrate for bonding.

Lamination Melt Coating

The adhesives of this invention can be used in any adhesive application,including but not limited to, disposables, packaging, laminates,pressure sensitive adhesives, tapes labels, wood binding, paper binding,non-wovens, road marking, reflective coatings, and the like.

In a preferred embodiment the adhesives of this invention can be usedfor disposable diaper and napkin chassis construction, elasticattachment in disposable goods converting, packaging, labeling,bookbinding, woodworking, and other assembly applications. Particularlypreferred applications include: baby diaper leg elastic, diaper frontaltape,, diaper standing leg cuff, diaper chassis construction, diapercore stabilization, diaper liquid transfer layer, diaper outer coverlamination, diaper elastic cuff lamination, feminine napkin corestabilization, feminine napkin adhesive strip, industrial filtrationbonding, industrial filter material lamination, filter mask lamination,surgical gown lamination, surgical drape lamination, and perishableproducts packaging.

The adhesives described above may be applied to any substrate. Preferredsubstrates include wood, paper, cardboard, plastic, thermoplastic,rubber, metal, metal foil (such as aluminum foil and tin foil),metallized surfaces, cloth, non-wovens (particularly polypropylene spunbonded fibers or non-wovens), spunbonded fibers, cardboard, stone,plaster, glass (including silicon oxide (SiO_(x))coatings applied byevaporating silicon oxide onto a film surface), foam, rock, ceramics,films, polymer foams (such as polyurethane foam), substrates coated withinks, dyes, pigments, PVDC and the like or combinations thereof.

Additional preferred substrates include polyethylene, polypropylene,polyacrylates, acrylics, polyethylene terephthalate, or any of thepolymers listed above as suitable for blends.

Any of the above substrates, and/or the polymers of this invention, maybe corona discharge treated, flame treated, electron beam irradiated,gamma irradiated, microwaved, or silanized.

The adhesives produced herein, when coated in some fashion between twoadherends, preferably perform such that the materials are held togetherin a sufficient fashion compared to a standard specification or astandard adhesive similarly constructed.

The polymer product of this invention may be used in any adhesiveapplication described in WO 97/33921 in combination with the polymersdescribed therein or in place of the polymers described therein.

The polymer product of this invention, alone or in combination withother polymers and or additives, may also be used to form hook and loopfasteners as described in WO 02/35956.

Characterization and Tests

Molecular weights (number average molecular weight (Mn), weight averagemolecular weight (Mw), and z-average molecular weight (Mz)) aredetermined using a Waters 150 Size Exclusion Chromatograph (SEC)equipped with a differential refractive index detector (DRI), an onlinelow angle light scattering (LALLS) detector and a viscometer (VIS). Thedetails of the detector calibrations have been described elsewhere[Reference: T. Sun, P. Brant, R. R. Chance, and W. W. Graessley,Macromolecules, Volume 34, Number 19, 6812-6820, (2001)]; attached beloware brief descriptions of the components.

The SEC with three Polymer Laboratories PLgel 10 mm Mixed-B columns, anominal flow rate 0.5 cm³/min, and a nominal injection volume 300microliters is common to both detector configurations. The varioustransfer lines, columns and differential refractometer (the DRIdetector, used mainly to determine eluting solution concentrations) arecontained in an oven maintained at 135° C.

The LALLS detector is the model 2040 dual-angle light scatteringphotometer (Precision Detector Inc.). Its flow cell, located in the SECoven, uses a 690 nm diode laser light source and (collects scatteredlight at two angles, 150 and 90°. Only the 150 output was used in theseexperiments. Its signal is sent to a data acquisition board (NationalInstruments) that accumulates readings at a rate of 16 per second. Thelowest four readings are averaged, and then a proportional signal issent to the SEC-LALLS-VIS computer. The LALLS detector is placed afterthe SEC columns, but before the viscometer.

The viscometer is a high temperature Model 150R (Viscotek Corporation).It consists of four capillaries arranged in a Wheatstone bridgeconfiguration with two pressure transducers. One transducer measures thetotal pressure drop across the detector, and the other, positionedbetween the two sides of the bridge, measures a differential pressure.The specific viscosity for the solution flowing through the viscometeris calculated from their outputs. The viscometer is inside the SEC oven,positioned after the LALLS detector but before the DRI detector.

Solvent for the SEC experiment was prepared by adding 6 grams ofbutylated hydroxy toluene (BHT) as an antioxidant to a 4 liter bottle of1,2,4 Trichlorobenzene (TCB)(Aldrich Reagent grade) and waiting for theBHT to solubilize. The TCB mixture was then filtered through a 0.7micron glass pre-filter and subsequently through a 0.1 micron Teflonfilter. There was an additional online 0.7 micron glass pre-filter/0.22micron Teflon filter assembly between the high pressure pump and SECcolumns. The TCB was then degassed with an online degasser (Phenomenex,Model DG-4000) before entering the SEC.

Polymer solutions were prepared by placing dry polymer in a glasscontainer, adding the desired amount of TCB, then heating the mixture at160° C. with continuous agitation for about 2 hours. All quantities weremeasured gravimetrically. The TCB densities used to express the polymerconcentration in mass/volume units are 1.463 g/ml at room temperatureand 1.324 g/ml at 135° C. The injection concentration ranged from 1.0 to2.0 mg/ml, with lower concentrations being used for higher molecularweight samples.

Prior to running each sample the DRI detector and the injector werepurged. Flow rate in the apparatus was then increased to 0.5 ml/minute,and the DRI was allowed to stabilize for 8-9 hours before injecting thefirst sample. The argon ion laser was turned on 1 to 1.5 hours beforerunning samples by running the laser in idle mode for 20-30 minutes andthen switching to full power in light regulation mode.

The branching index was measured using SEC with an on-line viscometer(SEC-VIS) and are reported as g′ at each molecular weight in the SECtrace. The branching index g′ is defined as:$g^{\prime} = \frac{\eta_{b}}{\eta_{l}}$where η_(b) is the intrinsic viscosity of the branched polymer and η_(l)is the intrinsic viscosity of a linear polymer of the sameviscosity-averaged molecular weight (M_(v)) as the branched polymer.η_(l)=KM_(v) ^(α), K and α are measured values for linear polymers andshould be obtained on the same SEC-DRI-LS-VIS instrument as the one usedfor branching index measurement. For polypropylene samples presented inthis invention, K=0.0002288 and α=0.705 were used. The SEC-DRI-LS-VISmethod obviates the need to correct for polydispersities, since theintrinsic viscosity and the molecular weight are measured at individualelution volumes, which arguably contain narrowly dispersed polymer.Linear polymers selected as standards for comparison should be of thesame viscosity average molecular weight and comonomer content. Linearcharacter for polymer containing C2 to C10 monomers is confirmed byCarbon-13 NMR the method of Randall (Rev. Macromol. Chem. Phys., C29(2&3), p. 285-297).

Linear character for C11 and above monomers is confirmed by GPC analysisusing a MALLS detector. For example, for a copolymer of propylene, theNMR should not indicate branching greater than that of the co-monomer(i.e. if the comonomer is butene, branches of greater than two carbonsshould not be present). For a homopolymer of propylene, the GPC shouldnot show branches of more than one carbon atom. When a linear standardis desired for a polymer where the comomoner is C9 or more, one canrefer to T. Sun, P. Brant, R. R. Chance, and W. W. Gratessley,Macromolecules, Volume 34, Number 19, 6812-6820, (2001) for protocols ondetermining standards for those polymers. In the case of syndiotacticpolymers, the standard should have a comparable amount of syndiotactictyas measured by Carbon 13 NMR.

In another embodiment the polymer produced by this invention has amolecular weight distribution (Mw/Mn) of at least 2, preferably at least5, preferably at least 10, even more preferably at least 20.

In another embodiment the polymer produced may have a unimodal, bimodal,or multimodal molecular weight distribution (Mw/Mn) distribution ofpolymer species as determined by Size Exclusion Chromatography (SEC). Bybimodal or multimodal is meant that the SEC trace has more than one peakor inflection points. An inflection point is that point where the secondderivative of the curve changes in sign (e.g., from negative to positiveor vice versus).

Peak melting point (Tm), peak crystallization temperature (Tc), heat offusion and crystallinity were determined using the following procedureaccording to ASTM E 794-85. Differential scanning calorimetric (DSC)data was obtained using a TA Instruments model 2920 machine. Samplesweighing approximately 7-10 mg were sealed in aluminum sample pans. TheDSC data was recorded by first cooling the sample to −50° C. and thengradually heating it to 200° C. at a rate of 10° C./minute. The sampleis kept at 200° C. for 5 minutes before a second cooling-heating cycleis applied. Both the first and second cycle thermal events are recorded.Areas under the curves were measured and used to determine the heat offusion and the degree of crystallinity. The percent crystallinity iscalculated using the formula, [area under the curve (Joules/gram)/B(Joules/gram)]*100, where B is the heat of fusion for the homopolymer ofthe major monomer component. These values for B are to be obtained fromthe Polymer Handbook, Fourth Edition, published by John Wiley and Sons,New York 1999. A value of 189 J/g (B) was used as the heat of fusion for100% crystalline polypropylene. For polymers displaying multiple meltingor crystallization peaks, the highest melting peak was taken as peakmelting point, and the highest crystallization peak was taken as peakcrystallization temperature.

The glass transition temperature (Tg) was measured by ASTM E 1356 usinga TA Instrument model 2920 machine.

Polymer samples for ¹³C NMR spectroscopy were dissolved ind₂-1,1,2,2-tetrachloroethane and the samples were recorded at 125° C.using a NMR spectrometer of 75 or 100 MHz. Polymer resonance peaks arereferenced to mmmm=21.8 ppm. Calculations involved in thecharacterization of polymers by NMR follow the work of F. A. Bovey in“Polymer Conformation and Configuration” Academic Press, New York 1969and J. Randall in “Polymer Sequence Determination, Carbon-13 NMRMethod”, Academic Press, New York, 1977. The percent of methylenesequences of two in length, %(CH₂)₂, were calculated as follows: theintegral of the methyl carbons between 14-18 ppm (which are equivalentin concentration to the number of methylenes in sequences of two inlength) divided by the sum of the integral of the methylene sequences ofone in length between 45-49 ppm and the integral of the methyl carbonsbetween 14-18 ppm, times 100. This is a minimum calculation for theamount of methylene groups contained in a sequence of two or more sincemethylene sequences of greater than two have been excluded. Assignmentswere based on H. N. Cheng and J. A. Ewen, Makromol. Chem. 1989, 190,1931.

Ethylene content of a polymer can be measured as follows. A thinhomogeneous film is pressed at a temperature of about 150° C. orgreater, then mounted on a Perkin Elmer PE 1760 infraredspectrophotometer. A full spectrum of the sample from 600 cm⁻¹ to 4000cm⁻¹ is recorded and the monomer weight percent of ethylene can becalculated. according to the following equation: Ethylene wt%=82.585−111.987X+30.045 X², wherein X is the ratio of the peak heightat 1155 cm⁻¹ and peak height at either 722 cm⁻¹ or 732 cm⁻¹, whicheveris higher. The concentrations of other monomers in the polymer can alsobe measured using this method.

Adhesive Testing

SAFT (modified D4498) measures the ability of a bond to withstand anelevated temperature rising at 10° F. (5.5° C.)/15 min., under aconstant force that pulls the bond in the shear mode. Bonds were formedin the manner described above (1 inch by 3 inch (2.5 cm×7.6 cm) (onKraft paper). The test specimens were suspended vertically in an oven atroom temperature with a 500 gram load attached to the bottom. Thetemperatures at which the weight fell was recorded (when the occasionalsample reached temperatures above the oven capacity >265° F. (129° C.)it was terminated and averaged in with the other samples at terminationtemperature).

Set time is defined as the time it takes for a compressed adhesivesubstrate construct to fasten together enough to give substrate fibertear when pulled apart, and thus the bond is sufficiently strong toremove the compression. The bond will likely still strengthen uponfurther cooling, however, it no longer requires compression. These settimes were measured by placing a molten dot of adhesive on to a filefolder substrate taped to a flat table. A file folder tab (1 inch by 3inch (2.5 cm×7.6 cm) was placed upon the dot 3 seconds later andcompressed with a 500 gram weight. The weight was allowed to sit forabout 0.5 to about 10 seconds. The construct thus formed was pulledapart to check for a bonding level good enough to produce substratefiber tear. The set time was recorded as the minimum time required forthis good bonding to occur. Standards were used to calibrate theprocess.

Once a construct has been produced it can be subjected to variousinsults in order to assess the effectiveness of the bond. Once a bondfails to a paper substrate a simple way to quantify the effectiveness isto estimate the area of the adhesive dot that retained paper fibers asthe construct failed along the bond line. This estimate is calledpercent substrate fiber tear. An example of good fiber, afterconditioning a sample for 15 hours at −12 ° C. and attempting to destroythe bond, would be an estimate of 80-100% substrate fiber tear. It islikely that 0% substrate fiber tear under those conditions would signala loss of adhesion.

Shore A hardness was measured according to ASTM 2240. An air cooled dotof adhesive was subjected to the needle and the deflection was recordedfrom the scale.

Dot T-Peel was determined according to ASTM D 1876, except that thespecimen was produced by combining two 1 inch by 3 inch (2.54 cm×7.62cm) substrate cut outs with a dot of adhesive with a volume that, whencompressed under a 500 gram weight occupied about 1 square inch of area(1 inch=2.54 cm). Once made all the specimens were pulled apart in sideby side testing (at a rate of 2 inches per minute) by a machine thatrecords the destructive force of the insult being applied. The maximumforce achieved for each sample tested was recorded and averaged, thusproducing the Average Maximum Force which is reported as the Dot T-Peel.

Adhesive Melt Viscosity (ASTM D-3236): Melt viscosity profiles aretypically measured at temperatures from 120° C. to 190° C. using aBrookfield Thermosel viscometer and a number 27 spindle.

Peel Strength (modified ASTM D1876): Substrates (1×3 inches (25×76 mm))are heat sealed with adhesive film (5 mils (130 μm) thickness) at 135°C. for 1 to 2 seconds and 40 psi (0.28 MPa) pressure. Bond specimenswere peeled back in a tensile tester at a constant crosshead speed of 2in/min (51 mm/min). The average force required to peel the bond (5specimens) apart is recorded.

Shear Adhesion Fail Temperature (SAFT) (modified ASTM D4498) measuresthe ability of the bond to withstand an elevated temperature rising at10° F. (5.5° C.)/15 min, under a constant force that pulls the bond inthe shear mode. Bonds 1 inch by 1 inch (Kraft paper) (25 mm×25 mm) wereformed of adhesive by heat sealing as in procedure “(b)” above for 1.5s. The test specimens were suspended vertically in an oven at 32° C.with a 500 g load attached to the bottom. The temperature at which theweight falls is recorded. Adhesives possessing high failure temperatureare essential for the assembly of packaging goods that are oftensubjected to very high temperatures during storage and shipping.

Peel Adhesion Failure Temperature (PAFT) was determined using followingprocedure modified according to the procedure of TAPPI T814 PM-77. Twosheets of 6″12″ Kraft paper were laminated together with a one inchstrip of molten adhesive heated to 177° C. The laminated sheet wastrimmed and cut into 1-inch wide strips. These strips were placed in anoven with a 100-gram of weight hanging in a peel mode. The overtemperature increased at a rate of 30° C. per hour. The sample were hungfrom a switch that trips when the samples fail to record the temperatureof failure.

Low Temperature Substrate Fiber Tear: Kraft paper bonds are prepared asin procedure “(b)” above. The bond specimens are placed in a freezer orrefrigerator to obtain the desired test temperature. The bonds areseparated by hand and a determination made as to the type of failureobserved. The amount of substrate fiber tear is expressed in percentage.“SF” indicates substrate failure.

Cloud point is determined by heating the adhesive blends to 121° C. andapplying a small bead (approximately 1 gram) of the molten adhesive tothe bulb of an ASTM thermometer. The temperature at which the moltenadhesive clouds over is then noted. These measures of cloud pointprovide an indication of a hot melt's overall compatibility, i.e., thecompatibility of the individual ingredients with each other.

Compression Molding: Plaques suitable for physical property testing werecompression molded on a Carver hydraulic press. 6.5 g of polymer wasmolded between brass plates (0.05″ thick) lined with Teflon™ coatedaluminum foil. A 0.033″ thick chase with a square opening 4″4″ was usedto control sample thickness. After one minute of preheat at 170° or 180°C., under minimal pressure, the hydraulic load was gradually increasedto ˜10,000-15,000 lbs., at which it was held for three minutes.Subsequently the sample and molding plates were cooled for three minutesunder ˜10,000 to 15,000 lbs. load between the water cooled platens ofthe press. Plaques were allowed to equilibrate at room temperature for aminimum of two days prior to physical property testing.

Unidirectional Tensile Testing: Dogbones for tensile testing were cutfrom compression molded plaques using a mallet handle die. Specimendimensions were those specified in ASTM D 1708. Tensile properties weremeasured on an Instron™ model 4502 equipped with a 22.48 lb. load celland pneumatic jaws fitted with serrated grip faces. Deformation wasperformed at a constant crosshead speed of 5.0 in/min with a datasampling rate of 25 points/second. Jaw separation prior to testing was0.876″, from which strains were calculated assuming affine deformation.Initial modulus, stress and strain at yield (where evident), peakstress, tensile strength at break, and strain at break were calculated.A minimum of five specimens from each plaque was tested, the resultsbeing reported as the average value. All stresses quoted were calculatedbased upon the original cross-sectional area of the specimen, taking noaccount of reduced cross-section as a function of increasing strain.

The rheological properties (G′, G″) were determined on ARES instrumentmanufactured by Rheometric Scientific, Piscataway, N.J. The polymerswere first melted and then cooled down at 1° C./min. Dynamic moduli wererecorded during the cooling, starting from a temperature higher than themelting point of the material by at least 30° C. down to about 80° C.The output of the test is therefore the evolution of the storage modulusG′, the loss modulus G″, as well as the ratio tanδ=G″/G′ as a functionof temperature. Measurements were made at a constant frequency of 10rad/s and 20 percent of strain, using a 12.5 mm diameter plate-and-plategeometry.

EXAMPLES General

All polymerizations were performed in a liquid filled, single-stagecontinuous reactor using mixed metallocene catalyst systems. The reactorwas a 0.5-liter stainless steel autoclave reactor and was equipped witha stirrer, a water cooling/steam heating element with a temperaturecontroller, and a pressure controller. Solvents, propylene, andcomonomers (such as butene and hexene), if present, were first purifiedby passing through a three-column purification system. The purificationsystem consists of an Oxiclear column (Model # RGP-R1-500 from Labclear)followed by a 5A and a 3A molecular sieve columns. Purification columnswere regenerated periodically whenever there is evidence of loweractivity of polymerization. Both the 3′A and 5A molecular sieve columnswere regenerated in-house under nitrogen at a set temperature of 260° C.and 315° C., respectively. The molecular sieve material was purchasedfrom Aldrich. Oxiclear column was regenerated in the originalmanufacture. Purified ethylene from in-house supply was fed into themanifold then the reactor through a Brookfield mass flow controller. Theethylene was delivered as a gas solubilized in the chilledsolvent/monomer mixture. The purified solvents and monomers were thenchilled to about −15° C. by passing through a chiller before fed intothe reactor through a manifold. Solvent and monomers were mixed in themanifold and fed into reactor through a single tube. All liquid flowrates are measured using Brooksfield mass flow meters or Micro-MotionCoriolis-type flow meters.

Unless otherwise noted the catalysts compounds were obtained formAlbemarle.

The catalyst compounds used to produce semi-crystalline polypropylenewere rac-dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dichloride,rac-dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl,rac-dimethylsilylbis(2-methylindenyl)zirconium dimethyl,rac-dimethylsilylbis(indenyl)hafnium dimethyl, andrac-1,2-ethylene-bis(4,7-dimethylindenyl)hafnium dimethyl (obtained fromBoulder Scientific Company).

The catalyst compounds used to produce amorphous polypropylene weredimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadenyl)(cyclododecylamido)titaniumdimethyl,dimethylsilyl(tert-butylamido)(tetramethylcyclopentadienyl)titaniumdimethyl(obtained from Boulder Scientific Company),[di(p-triethylsilylphenyl)methylene](cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdimethyl(produced according to the examples in U.S. Pat. No. 6,528,670)and dimethylsilyl(tetramethylcylopentadienyl)(N-1-adamantyl)titaniumdimethyl (produced according to the examples in U.S. Pat. No.5,955,625).

Dimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdichloride was made according to the examples in U.S. Pat. No.5,057,475. The dimethyl version was obtained by dimethylation of thedichloride version.

Rac-Dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dichloride anddimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdichloride were activated with MAO (methylalumoxane).Rac-1,2-ethylenebis(4,7-dimethylindenyl)hafnium dimethyl waspreactivated with trityl tetrakis(pentafluorophenyl)borate (obtainedfrom Single-Site Catalysts, LLC). The rest of the catalysts werepreactivated with N,N-dimethylaniliniumtetrakis(pentafluorophenyl)borate(obtained from Albemarle). For catalystsystems with preactivation, the catalysts were activated with cocatalystat a molar ratio of 1:1 to 1:1.1 in 700 ml of toluene at least 10minutes prior to the polymerization reaction. The catalyst systems werediluted to a concentration of catalyst ranging from 0.2 to 1.4 mg/ml intoluene. The catalyst solution was used for all polymerization runscarried out in the, same day. New batch of catalyst solution wasprepared in case that more than 700 ml of catalyst solution was consumedin one day. Each catalyst solution was pumped through separate lines.Catalysts were mixed in a manifold, and then fed into the reactorthrough a single line. In methylalumoxane activated systems, 280 ml ofmethylalumoxane (MAO, 10 wt. % in toluene, from Albemarle) was dilutedin 1000 ml of toluene, and the solution was stored in a 5-literstainless cylinder. Catalysts were diluted to a concentration rangingfrom 0.2 to 1.4 mg/ml in toluene. Each catalyst solution and themethylalumoxane solution were pumped through separate lines. Catalystsand MAO were mixed in a manifold, and then fed into the reactor througha single line. The connecting tube between the catalyst manifold andreactor inlet was about 1 meter long.

All catalyst solutions were kept in an inert atmosphere with <1.5 ppmwater content and fed into reactor by metering pumps. Catalyst andmonomer contacts took place in the reactor. Catalyst pumps werecalibrated periodically using toluene as the calibrating medium.Catalyst concentration in the feed was controlled through changing thecatalyst concentration in catalyst solution and/or changing in thepumping rate of catalyst solution. The pumping rate of catalyst solutionvaried in a range of 0.2 to 5 ml/minute.

As an impurity scavenger, 55 ml of tri-iso-butyl aluminum (25wt. % intoluene, Akzo Noble) was diluted in 22.83 kilogram of hexane. Thediluted tri-iso-butyl aluminum solution was stored in a 37.9-litercylinder under nitrogen blanket. The solution was used for allpolymerization runs until about 90% of consumption, then a new batch wasprepared. Pumping rates of the tri-iso-butyl aluminum solution variesfrom polymerization reaction to reaction, ranging from 0 (no scavenger)to 4 ml per minutes.

For polymerization reactions involving alpha, omega-dienes,1,9-decadiene was diluted to a concentration ranging from 4.8 to 9.5vol. % in toluene. The diluted solution was then fed into reactor by ametering pump through a comonomer line. (The 1,9-decadiene was obtainedfrom Aldrich and was purified by first passing through alumina activatedat high temperature under nitrogen, followed by molecular sieveactivated at high temperature under nitrogen.)

The reactor was first (cleaned by continuously pumping solvent (e.g.,hexane) and scavenger through the reactor system for at least one hourat a maximum allowed temperature (about 150° C.). After cleaning, thereactor was heated/cooled to the desired temperature using water/steammixture flowing through the reactor jacket and controlled at a setpressure with controlled solvent flow. Monomers and catalyst solutionswere then fed into the reactor when a steady state of operation wasreached. An automatic temperature control system was used to control andmaintain the reactor at a set temperature. Onset of polymerizationactivity was determirned by observations of a viscous product and lowertemperature of water-steam mixture. Once the activity was establishedand system reached equilibrium, the reactor was lined out by continuingoperating the system under the established condition for a time periodof at least five times of mean residence time prior to samplecollection. The resulting mixture, containing mostly solvent, polymerand unreacted monomers, was collected in a collection box after thesystem reached a steady state operation. The collected samples werefirst air-dried in a hood to evaporate most of the solvent, and thendried in a vacuum oven at a temperature of about 90° C. for about 12hours. The vacuum oven dried samples were weighed to obtain yields. Allthe reactions were carried out at a pressure of 2.41 MPa-g and in thetemperature range of 45 to 130° C.

Examples 1-4

Four samples were made withrac-dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl anddimethylsilyl(tetramethylcyclopentadienyl) (cyclododecylamido)titaniumdimethyl at a temperature 115° C. over a range of catalyst ratios. Thepolymerization reactions followed the general procedure described above.The detailed experimental conditions and results are presented inTable 1. TABLE 1 Example 1 2 3 4 Catalyst #1 A A A A Catalyst #1 feedrate 4.83E−06 3.66E−06 3.00E−06 2.68E−06 (mole/min) Catalyst #2 B B B BCatalyst #2 feed rate 3.64E−07 3.64E−07 3.64E−07 3.64E−07 (mole/min)Propylene feed rate 14 14 14 14 (g/min) Hexane feed rate 90 90 90 90(ml/min) Polymerization temp 115 115 115 115 (° C.) Mn (kg/mol) 19.118.2 16.4 16.9 Mw (kg/mol) 31 28.3 25.7 26.7 Mz (kg/mol) 66.1 52.4 46.953.1 g′ @ Mz 1.02 0.99 0.96 0.9 Tc (° C.) 90.5 98.8 97.7 97.1 Tm (° C.)140.5 143.2 143.8 142.8 Tg (° C.) −17.7 −10.4 −10.4 −11.3 Heat of fusion(J/g) 21.7 25.7 34.7 35.1 Viscosity @190° C. 1540 1340 1240 798 (cps)Conversion (%) 95.3 89.6 87.1 92.8 Catalyst activity 5.7 6.9 8.0 9.4 (kgpolymer/g catalyst)Catalysts:A = dimethylsilyl (tetramethylcyclopentadienyl) (cyclododecylamido)titanium dimethylB = rac-dimethylsilyl bis(2-methyl-4-phenylindenyl) zirconium dimethyl

Examples 5-8

Four samples were made withrac-dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl anddimethylsilyl(tetramethylcyclopentadienyl)(t-butylamido)titaniumdimethyl at a temperature of 100° C. over a range of catalyst ratio. Thepolymerization reactions followed the general procedure described above.The detailed experimental conditions and results are presented in Table2. TABLE 2 Example 5 6 7 8 Catalyst #1 F F F F Catalyst #1 feed rate4.92E−06 4.92E−06 4.92E−06 4.92E−06 (mole/min) Catalyst #2 B B B BCatalyst #2 feed rate 5.67E−07 8.50E−07 1.13E−06 1.42E−06 (mole/min)Propylene feed rate 14 14 14 14 (g/min) Hexane feed rate 90 90 90 90(ml/min) Polymerization 100 100 100 100 temperature (° C.) Mn (kg/mol)12.1 11.9 8.8 12.4 Mw (kg/mol) 29.4 30.7 26.3 28 Mz (kg/mol) 84.3 81.680.7 84.7 g′ @ Mz 0.93 0.88 0.87 0.84 Tc (° C.) 95.8 98.4 96.1 95.8 Tm(° C.) 145.2 145.7 143.3 143.0 Tg (° C.) −9.6 −10.4 −11.1 −10.0 Heat offusion (J/g) 21.4 32.4 30.0 33.0 Viscosity @190° C. 1100 1040 840 675(cps) Conversion (%) 88.63 91.73 68.09 77.23 Catalyst activity 6.38 6.084.18 4.42 (kg polymer/g catalyst)Catalysts:B = rac-dimethylsilyl bis(2-methyl-4-phenylindenyl) zirconium dimethylF = dimethylsilyl(tetramethylcyclopentadienyl)(tert-butylamido) titaniumdimethyl

Examples 9-15

Seven samples were made with dimethylsilylbis(indenyl)hafnium dimethyland dimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titanium dimethyl over a range of temperatures. Thepolymerization reactions followed the general procedure described above.The detailed experimental conditions and results are presented in Table3. The data show that temperature has appreciable effects oncrystallinity, Mw, Mw/Mn, and level of branching. The population canalso be manipulated through reaction temperatures since the reactionkinetics of each catalyst has unique response to polymerizationtemperatures. TABLE 3 Example 9 10 11 12 13 14 15 Catalyst #1 A A A A AA A Catalyst #1 5.22E−06 5.22E−06 5.22E−06 5.22E−06 5.22E−06 5.22E−065.22E−06 feed rate (mole/min) Catalyst #2 C C C C C C C Catalyst #21.31E−06 1.31E−06 1.31E−06 1.31E−06 1.31E−06 1.31E−06 1.31E−06 feed rate(mole/min) Propylene 14 14 14 14 14 14 14 feed rate (g/min) Hexane feed90 90 90 90 90 90 90 rate (ml/min) Polymerization 110 105 100 95 90 8580 temperature (° C.) Mn (kg/mol) 8.5 8.2 9.8 11.1 22.5 26.6 30.9 Mw(kg/mol) 15.7 17.1 19.8 23.5 41.1 46.9 55.8 Mz (kg/mol) 30.6 37.9 42.240.4 79.8 84.8 95.5 g′ @Mz 1 0.97 0.95 0.97 0.98 0.97 0.98 Tc (° C.)22.8 31.6 40.5 47.8 53.5 61.0 64.8 Tm (° C.) 74.7 82.3 87.4 94.3 103.3107.7 113.7 Tg (° C.) −15.5 −13.0 −12.0 −10.0 −7.5 −7.5 −6.0 Heat offusion 14.4 16.6 21.5 26.0 21.0 27.8 26.7 (J/g) Viscosity 227 272 441813 5280 7250 15400 @ 190° C. (cps)Catalysts:A = dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)titanium dimethylC = rac-dimethylsilyl bis (indenyl) hafnium dimethyl

Examples 16-19

Four samples were made with rac-dimethylsilylbis(indenyl)hafniumdimethyl anddimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl at a temperature of 100° C. and various catalyst ratios. Thepolymerization reactions followed the general procedure described above.The detailed experimental conditions and results are presented in Table4. The data show that catalyst ratios have appreciable effects oncrystallinity, Mw, Mw/Mn, and level of branching. The population canalso be manipulated through reaction temperatures since the reactionkinetics of each catalyst has unique response to polymerizationtemperatures. TABLE 4 Example 16 17 18 19 Catalyst #1 A A A A Catalyst#1 feed rate 8.49E−07 8.49E−07 8.49E−07 8.49E−07 (mole/min) Catalyst #2C C C C Catalyst #2 feed rate 5.51E−07 8.26E−07 1.28E−06 1.93E−06(mole/min) Propylene feed rate 14 14 14 14 (g/min) Hexane feed rate 9090 90 90 (ml/min) Polymerization 100 100 100 100 temperature (° C.) Mn(kg/mol) 17.1 14.1 9.6 7.3 Mw (kg/mol) 28 20.7 14.3 10.6 Mz (kg/mol) 6537.6 24.9 18.2 g′ @ Mz 1.05 0.97 0.92 0.94 Tc (° C.) 61.2 55.2 30.8 28.8Tm (° C.) 107.3 97.6 76.9 64.3 Tg (° C.) −8.9 −14.5 −15.3 −14.6 Heat offusion (J/g) 29.9 31.2 19.9 7.6 Viscosity @ 190° C. 1355 412 165 87(cps) Conversion (%) 86.20 91.89 100.56 97.90 Catalyst activity 18.7416.49 13.97 10.34 (kg polymer/g catalyst)Catalysts:A = dimethylsilyl (tetramethylcyclopentadienyl) (cyclododecylamido)titanium dimethylC = rac-dimethylsilyl bis (indenyl) hafnium dimethyl

Examples 20-34

Fifteen samples were made withrac-dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl anddimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl catalysts, following the general procedure described above withthe exception that a small quantity of 1,9-decadiene was fed as thediolefin monomer along with propylene as the alpha-olefin monomer. Thedetailed experimental conditions and results are presented in Tables 5and 6. TABLE 5 Example 20 21 22 23 24 Catalyst #1 A A A A A Catalyst #16.53E−06 6.53E−06 6.53E−06 6.53E−06 6.53E−06 feed rate (mole/min)Catalyst #2 B B B B B Catalyst #2 6.92E−07 3.64E−07 3.64E−07 2.19E−072.19E−07 feed rate (mole/min) Propylene feed 14 14 14 8.3 10 rate(g/min) 1,9 decadiene 0.19 0.19 0.19 0.13 0.13 feed rate (ml/min) Hexanefeed 90 90 90 90 90 rate (ml/min) Polymerization 120 125 120 120 110temperature (° C.) Mn (kg/mol) 15.6 14.7 14.3 — — Mw (kg/mol) 23 24.629.5 — — Mz (kg/mol) 55.2 64.2 85 — — g′ @Mz 0.85 0.91 0.85 — — Tc (°C.) 86.5 91.8 91.8 86.5 87.6 Tm (° C.) 116.6 128.7 129.7 128.8 137.6 Tg(° C.) −10.6 −11.1 −9.7 −9.4 −7.5 Heat of fusion 31.8 32.1 26.0 17.019.4 (J/g) Viscosity 721 725 1240 448 2240 @ 190° C. (cps) Conversion(%) 93.32 77.57 81.12 77.49 85.13 Catalyst activity 4.00 3.54 3.70 2.152.85 (kg polymer/g catalyst) Example 25 26 27 28 29 Catalyst #1 A A A AA Catalyst #1 5.22E−06 5.22E−06 5.22E−06 6.53E−06 6.53E−06 feed rate(mole/min) Catalyst #2 B B B B B Catalyst #2 7.65E−07 7.65E−07 7.65E−072.19E−07 4.74E−07 feed rate (mole/min) Propylene feed 14 14 14 10 14rate (g/min) 1,9 decadiene 0.24 2.24 0.19 0.13 0.19 feed rate (ml/min)Hexane feed 90 90 90 90 90 rate (ml/min) Polymerization 115 117 110 125115 temperature (° C.) Mn (kg/mol) 20 23 17.3 Mw (kg/mol) 36.7 45.5 34.5Mz (kg/mol) 111.9 104 97.1 g′ @Mz 0.68 0.75 0.75 Tc (° C.) 91.1 87.096.8 77.3 88.5 Tm (° C.) 136.6 133.7 134.2 130.0 136.3 Tg (° C.) −9.6−10.7 −9.7 −11.2 −12.4 Heat of fusion 51.5 39.5 42.5 15.1 35.8 (J/g)Viscosity 880 518 1850 661 1040 @ 190° C. (cps) Conversion (%) 92.2089.30 96.84 80.62 91.15 Catalyst activity 4.72 4.57 4.96 2.70 4.07 (kgpolymer/g catalyst)Catalysts:A = dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)titanium dimethylB = rac-dimethylsilyl bis(2-methyl-4-phenylindenyl) zirconium dimethyl

TABLE 6 Example 30 31 32 33 34 Catalyst #1 A A A A A Catalyst #11.02E−06 5.22E−06 6.53E−06 6.53E−06 6.53E−06 feed rate (mole/min)Catalyst #2 B B B B B Catalyst #2 1.13E−07 7.65E−07 4.74E−07 6.20E−073.64E−07 feed rate (mole/min) Propylene feed 14 14 14 14 14 rate (g/min)1,9 decadiene 0.19 0.24 0.19 0.19 0.19 feed rate (ml/min) Hexane feed 9090 90 90 90 rate (ml/min) Polymerization 115 115 110 110 115 temperature(° C.) Mn (kg/mol) 20.3 14.9 13.6 16.1 17.6 Mw (kg/mol) 96.2 34.3 30.230.4 36.5 Mz (kg/mol) 636.2 114.8 67.6 68.7 91.5 g′ @Mz 0.46 0.72 0.950.88 0.85 Tc (° C.) 91.4 91.8 94.3 84.4 Tm (° C.) 129.3 140.5 140.6137.2 Tg (° C.) −10.0 −11.2 −8.9 −8.2 Heat of fusion 46.9 28.3 38.4 20.8(J/g) Viscosity 1030 1870 1360 2470 @ 190° C. (cps) Conversion (%) 56.3895.32 97.29 97.24 87.82 Catalyst activity 15.44 4.88 4.34 4.23 4.00 (kgpolymer/g catalyst)Catalysts:A = dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)titanium dimethylB = rac-dimethylsilyl bis(2-methyl-4-phenylindenyl) zirconium dimethyl

Examples 35-39

Five samples were made with dimethylsilylbis (indenyl)hafnium dimethylanddimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl over a range of temperatures from 85 to 105° C., following thegeneral procedure described above with the exception that a smallquantity of 1,9-decadiene was fed as the diolefin monomer along withpropylene as the alpha-olefin monomer. The detailed experimentalconditions and results are presented in Table 7. TABLE 7 Example 35 3637 38 39 Catalyst #1 A A A A A Catalyst #1 5.22E−06 5.22E−06 5.22E−065.22E−06 5.22E−06 feed rate (mole/min) Catalyst #2 C C C C C Catalyst #21.75E−05 1.75E−06 1.75E−06 1.75E−06 1.75E−06 feed rate (mole/min)Propylene feed 14 14 14 14 14 rate (g/min) 1,9 decadiene 0.24 0.24 0.240.24 0.24 feed rate (ml/min) Hexane feed 90 90 90 90 90 rate (ml/min)Polymerization 105 100 95 90 85 temperature (° C.) Mn (kg/mol) 9.6 15.714.1 15.2 29.3 Mw (kg/mol) 16.5 24.6 30 40.4 69.1 Mz (kg/mol) 33.4 48.470.7 103.1 222.6 g′ @ Mz 0.89 0.81 0.8 0.76 0.66 Tc (° C.) 25.2 29.430.9 41.8 53.5 Tm (° C.) 67.3 76.1 81.2 91.3 102.3 Tg (° C.) −15.4 −13.3−13.1 −8.1 −7.4 Heat of fusion 13.4 19.5 20.9 25.7 33.3 (J/g) Viscosity194 291 568 1650 5210 @ 190° C. (cps)Catalysts:A = dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)titanium dimethylC = rac-dimethylsilyl bis (indenyl) hafnium dimethyl

Examples 40-43

Four samples were made with rac-dimethylsilylbis(indenyl)hafniumdimethyl anddimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl, following the general procedure described above with theexception that a small quantity of 1,9-decadiene was fed as the diolefinmonomer along with propylene as the alpha-olefin monomer. The detailedexperimental conditions and results are presented in Table 8. TABLE 8Example 40 41 42 43 Catalyst #1 A A A A Catalyst #1 feed rate 8.49E−078.49E−07 8.49E−07 5.22E−06 (mole/min) Catalyst #2 C C C C Catalyst #2feed rate 8.26E−07 5.51E−07 5.51E−07 5.82E−07 (mole/min) Propylene feedrate 14 14 14 14 (g/min) 1,9 decadiene feed rate 0.05 0.02 0.05 0.19(ml/min) Hexane feed rate 90 90 86 90 (ml/min) Polymerization 100 95 9095 temperature (° C.) Mn (kg/mol) 10.5 16.1 23 28.3 Mw (kg/mol) 19.524.4 39.4 94.8 Mz (kg/mol) 38 44.3 71.3 455.2 g′ @Mz 0.92 0.93 0.93 0.54Tc (° C.) 47.7 53.7 71.0 37.4 Tm (° C.) 94.4 98.6 112.5 101.2 Tg (° C.)−12.3 −11.1 −24.6 −10.3 Heat of fusion (J/g) 30.8 31.6 44.6 22.4Viscosity @ 190° C. 327 625 2370 — (cps) Conversion (%) 93.80 — 98.62 —Catalyst activity 16.83 — 21.44 — (kg polymer/g catalyst)Catalysts:A = dimethylsilyl (tetramethylcyclopentadienyl) (cyclododecylamido)titanium dimethylC = rac-dimethylsilyl bis (indenyl) hafnium dimethyl

Examples 44-47

Four samples were made usingrac-1,2-ethylene-bis(4,7-dimethylindenyl)hafnium dimethyl anddimethylsilyl-(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl at a temperature 10° C. over a range of catalyst ratios. Theconditions used for examples 44 to 47, which included diolefinincorporation, followed the general procedure described above with theexception that a small quantity of 1,9-decadiene was fed as the diolefinmonomer along with propylene as the alpha-olefin monomer. The detailedexperimental conditions and results are presented in Table 9. TABLE 9Example 44 45 46 47 Catalyst #1 A A A A Catalyst #1 feed rate 6.53E−063.79E−06 2.74E−06 2.09E−06 (mole/min) Catalyst #2 D D D D Catalyst #2feed rate 4.25E−07 4.25E−07 4.25E−07 4.25E−07 (mole/min) Propylene feedrate 14 14 14 14 (g/min) 1,9 decadiene feed rate 0.09 0.09 0.09 0.09(ml/min) Hexane feed rate 90 90 90 90 (ml/min) Polymerization 115 115115 115 temperature (° C.) Mn (kg/mol) 21.5 20 21.2 16.1 Mw (kg/mol)36.2 32.7 34 33.5 Mz (kg/mol) 100.1 95.6 123.7 128.8 Tc (° C.) 41.0 51.559.8 74.4 Tm (° C.) 94.3 97.6 103.4 109.4 Tg (° C.) −22.8 −23.8 −12.5−18.9 Heat of fusion (J/g) 4.1 6.8 11.3 15.8 Viscosity @ 190° C. 20901750 1570 1230 (cps) Conversion (%) 83.58 83.95 71.84 63.10 Catalystactivity 3.80 6.26 7.08 7.78 (kg polymer/g catalyst)Catalysts:A = dimethylsilyl (tetramethylcyclopentadienyl) (cyclododecylamido)titanium dimethylD = rac-1,2-ethylene bis (4,7-dimethylindenyl)hafnium dimethyl

Examples 48-51

Four samples were made withrac-dimethylsilylbis(2-methylindenyl)zirconium dimethyl anddimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl at a temperature of 80° C., following the general proceduredescribed above with the exception that a small quantity of1,9-decadiene was fed as the diolefin monomer along with propylene asthe alpha-olefin monomer. The detailed experimental conditions andresults are presented in Table 10. TABLE 10 Example 48 49 50 51 Catalyst#1 A A A A Catalyst #1 feed rate 6.53E−06 6.53E−06 6.53E−06 6.53E−06(mole/min) Catalyst #2 E E E E Catalyst #2 feed rate 1.23E−06 1.57E−061.92E−06 2.26E−06 (mole/min) Propylene feed rate 14 14 14 14 (g/min) 1,9decadiene feed rate 0.14 0.14 0.14 0.14 (ml/min) Hexane rate (ml/min) 9090 90 90 Polymerization 80 80 80 80 temperature (° C.) Mn (kg/mol) 19.916 11.4 10 Mw (kg/mol) 43.8 36.9 25.9 19.2 Mz (kg/mol) 106.3 72.3 54.538.8 g′ @ Mz 0.88 0.93 0.93 0.93 Tc (° C.) 49.0 53.3 58.6 53.1 Tm (° C.)109.9 107.8 103.2 102.0 Tg (° C.) −10.7 −7.4 −9.1 −9.6 Heat of fusion(J/g) 25.8 29.4 31.4 37.7 Viscosity @ 190° C. 4680 2040 952 464 (cps)Catalysts:A = dimethylsilyl (tetramethylcyclopentadienyl) (cyclododecylamido)titanium dimethylE = rac-dimethylsily bis(2-methylindenyl)zirconium dimethyl

Examples 52-57

Six samples were made withrac-dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl anddimethylsilyl-(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl at a temperature range of 80 to 95° C., following the generalprocedure described above with the exception that (1) a small quantityof 1,9-decadiene was fed as the diolefin monomer along with propylene asthe alpha-olefin monomer; (2) A small amount of hydrogen was also fed inthe reactor. The detailed experimental conditions and results arepresented in Table 11. Examples 52-57 show that addition of hydrogen caneffectively manipulate Mw, Mw/Mn, crystallinity, the ratio ofcrystalline phase to the amorphous phase, in addition to the controlobtained through catalyst selections and process conditions such astemperatures. TABLE 11 Example 52 53 54 55 56 57 Catalyst #1 A A A A A ACatalyst #1 6.10E−06 6.10E−06 6.10E−06 6.10E−06 6.10E−06 6.10E−06 feedrate (mole/min) Catalyst #2 B B B B B B Catalyst #2 2.83E−07 2.83E−072.83E−07 2.83E−07 1.98E−07 1.98E−07 feed rate (mole/min) Propylene 14 1414 14 14 14 (g/min) 1,9 decadiene 0.19 0.19 0.19 0.19 0.19 0.19 feedrate (ml/min) H2 feed rate 50 50 50 50 70 70 (cc/min) Hexane feed 90 9090 90 90 90 rate (ml/min) Polymerization 95 90 85 80 90 80 temperature(° C.) Mn (kg/mol) 12.6 11 12.5 15.7 18.1 11.7 Mw (kg/mol) 27.5 43.242.3 85.3 34 29.8 Mz (kg/mol) 72.2 127 153.4 468.3 126 99 g′ @ Mz 0.820.74 0.8 0.66 0.8 0.84 Tc (deg C.) 95.7 95.8 97.4 97.0 98.9 97.7 Tm (°C.) 141.0 145.1 145.8 147.0 144.5 145.1 Tg (° C.) −14.6 −13.3 −12.3 −9.8−17.2 −14.8 Heat of fusion 38.5 45.4 35.9 35.4 49.3 39.2 (J/g) Viscosity668 1049 2148 16090 810 822 @ 190° C. (cps)Catalysts:A = dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)titanium dimethylB = rac-dimethylsilyl bis(2-methyl-4-phenylindenyl) zirconium dimethyl

Examples 58-60

Three samples were made with rac-dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl anddimethylsilyl-(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl at a temperature 115° C. and a catalyst ratio of about 87 molarpercent, following the general procedure described above with thefollowing exceptions: (1) a small quantity of 1,9-decadiene was fed asthe diolefin monomer; (2) bothrac-dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl anddimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl catalysts were premixed and diluted in toluene, then fed intocatalyst manifold without preactivation; (3) N,N-dimethylaniliniumtetrakis(pentafluorophenyl)borate was diluted in toluene and then fedinto catalyst manifold; (4) catalyst activation started in catalystmanifold. The detailed experimental conditions and results are presentedin Table 12. Examples 58-60 demonstrate that catalysts can be activatedin-line just prior to the reactor and in reactor. TABLE 12 Example 58 5960 Catalyst #1 A A A Catalyst #1 feed rate (mole/min) 4.06E−06 2.54E−061.52E−06 Catalyst #2 B B B Catalyst #2 feed rate (mole/min) 2.95E−071.84E−07 1.11E−07 Propylene (g/min) 14 14 14 1,9 decadiene feed rate(ml/min) 0.14 0.14 0.14 Hexane feed rate (ml/min) 90 90 90Polymerization temperature (° C.) 115 115 115 Mn (kg/mol) 13.2 18.2 24.2Mw (kg/mol) 34.5 50.8 69.9 Mz (kg/mol) 99.6 169 248.6 g′ @ Mz 0.79 0.720.69 Tc (° C.) 90.6 92.9 93.0 Tm (° C.) 137.0 139.6 142.6 Tg (° C.)−10.8 −10.0 −8.7 Heat of fusion (J/g) 32.5 32.9 28.4 Viscosity @190° C.(cps) 1657 3170 11600 Conversion (%) 89.64 77.50 95.59 Catalyst activity(kg polymer/g 6.43 8.90 18.29 catalyst)Catalysts:A = dimethylsilyl (tetramethylcyclopentadienyl) (cyclododecylamido)titanium dimethylB = rac-dimethylsilyl bis(2-methyl-4-phenylindenyl) zirconium dimethyl

Examples 61-66

Six samples were made with dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl anddimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl at a temperature range of 105 to 130° C. and a catalyst mix ofabout 35.6 molar percent, following the general procedure describedabove with the following exceptions: (1) a small quantity of1,9-decadiene was fed as the diolefin monomer; (2) ethylene was added tothe reactor. The detailed experimental conditions and results arepresented in Table 13. Ethylene content in the polymer was obtained fromby Fourier Transformation Infrared analysis (FTIR). TABLE 13 Example 6162 63 64 65 66 Catalyst #1 A A A A A A Catalyst #1 1.02E−06 1.02E−061.02E−06 1.02E−06 1.02E−06 1.02E−06 feed rate (mole/min) Catalyst #2 B BB B B B Catalyst #2 1.84E−07 1.84E−07 1.84E−07 1.84E−07 1.84E−071.84E−07 feed rate (mole/min) Propylene 20 20 20 20 20 20 feed rate(g/min) 1,9 decadiene 0.186 0.186 0.186 0.186 0.186 0.186 feed rate(ml/min) Ethylene feed 0.2 0.2 0.2 0.2 0.2 0.2 rate (SLPM) Hexane feed90 90 90 90 90 90 rate (ml/min) Polymerization 130 125 120 115 110 105temperature (° C.) Mn (kg/mol) 13.1 12.3 11.8 15.1 15.3 17.7 Mw (kg/mol)37.3 36.2 40.5 47.7 45.2 53.8 Mz (kg/mol) 149.2 122 132.1 153.9 206.8180.7 g′ @ Mz 0.67 0.65 0.63 0.61 0.56 0.56 Tc (° C.) 80.4 79.6 84.685.5 87.7 86.6 Tm (° C.) 121.8 121.9 124.6 125.2 126.1 126.2 Tg (° C.)−15.0 −15.2 −14.9 −14.8 −15.0 −15.6 Heat of fusion 32.4 43.3 51.7 50.550.4 49.7 (J/g) Viscosity 1440 977 1090 1510 1530 1720 @ 190° C. (cps)Ethylene content 4.3 3.5 3 2.6 2.9 2.9 from FTIR (wt. %) Conversion (%)68.11 82.57 89.87 92.79 92.18 Catalyst activity 24.92 30.21 32.88 33.9533.73 (kg polymer/g catalyst)Catalysts:A = dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)titanium dimethylB = rac-dimethylsilyl bis(2-methyl-4-phenylindenyl) zirconium dimethyl

Examples 67-71

All these samples were made withdimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl anddimethylsilyl-(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl at a temperature range of 105 to 115° C. except example 69,following the general procedure described above with the followingexceptions: (1) a small quantity of dicyclopentadiene was used inexample 67 (The dicyclopentadiene, obtained from aldrich, was firstdissolved in toluene. The solution was then purified by passing throughalumina activated at high temperature under nitrogen, followed bymolecular sieve activated at high temperature under nitrogen.); (2)1-butene was used in examples 68 and 70; (3) 1,9-(1-decadiene and1-hexene were fed as the diolefin monomer and comonomer, respectively inexample 71. Example 69 was made usingdimethylsilyl-(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl and rac-dimethylsily bis(2-methylindenyl)zirconium dimethylcatalysts. The detailed experimental conditions and results arepresented in Table 14. TABLE 14 Example 67 68 69 70 71 Catalyst #1 A A AA A Catalyst #1 5.22E−06 5.22E−06 2.09E−06 5.22E−06 5.22E−06 feed rate(mole/min) Catalyst #2 B B E B B Catalyst #2 7.65E−07 7.65E−07 4.25E−077.65E−07 7.65E−07 feed rate (mole/min) Propylene 14 14 14 14 14 feedrate (g/min) Comonomer dicyclo- Butene-1 — Butene-1 1,9 pentadienedecadiene Comonomer 0.23 0.6 — 2.5 0.206 feed rate (ml/min) 1-hexene — —— — 3.29 flow rate (ml/min) Hexane feed 90 90 90 90 90 rate (ml/min)Polymerization 110 115 110 105 115 temperature (° C.) Mn (kg/mol) — —12.2 — — Mw (kg/mol) — — 30.6 — — Mz (kg/mol) — — 84.3 — — Tc (° C.) — —72.3 86.0 42.6 Tm (° C.) — — 112.1 124.8 89.8 Tg (° C.) — — −22.4 −12.3−15.2 Heat of fusion — — 23.3 38.4 27.0 (J/g) Viscosity 665 563 14201100 524 @ 190° C. (cp) Conversion (%) 74.40 98.07 65.78 — 98.98Catalyst activity 3.81 5.15 8.11 — 5.77 (kg polymer/g catalyst)CatalystsA = dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)titanium dimethylB = rac-dimethylsilyl bis(2-methyl-4-phenylindenyl) zirconium dimethyl

Example 72

Example 72 was carried out in a 500-ml autoclave batch reactor. 125 mlof purified toluene was first added into the stainless steel autoclavereactor, followed by addition of 0.1 ml of tri-iso-butyl aluminum(TIBAL) solution (25-wt. % of TIBAL diluted in 5 ml of toluene). Themixture was then stirred and heated to 120° C. until stable pressure.The reactor was maintained at a slightly positive pressure. Insuccession, 125 ml of prepurified propylene was added under stirring.The reactor mixture was heated to 120° C. At this reactor temperature,1.5 ml of the premixed and preactivated catalyst solution was cannulatedinto the reactor using nitrogen. The catalyst solution consists of 32 mgof dimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl, 1.9 mg ofrac-dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl, and1.6 mg of dimethylsilylbis(indenyl)hafnium dimethyl, and 62.1 mg ofN,N-dimethylanilinium tetrakis(pentafluorophenyl)borate were dissolvedin 50 ml of toluene. The polymerization was conducted for 15 minutes.Thereafter, the reactor was cooled down and vented to the atmosphere.The resulting mixture, containing mostly solvent, polymer and unreactedmonomers, was collected in a collection box and first air-dried in ahood to evaporate most of the solvent, and then dried in a vacuum ovenat a temperature of about 90 ° C. for about 12 hours. The resultingpolymer (12.79 grams) showed a peak crystallization temperature by DSCof 102.9° C., a glass transition (Tg) of −8.7° C., and a heat of fusionof 51.9 J/g. The average molecular weights, Mn/Mw/Mz, are33825/66387/267680.

Example 73-75 (Comparative)

Three samples were made withrac-dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl ordimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl, following the general procedure described above except thatonly one catalyst was used.Rac-dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl vasused to make isotactic polypropylene, whiledimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdimethyl was used to make amorphous polypropylene. The experimentalconditions and viscosity of polymer samples are presented in Table 15.TABLE 15 Example 73 74 75 Catalyst A A B Catalyst feed rate (mol/min)5.08E−06 5.08E−06 5.67E−07 Propylene feed rate (g/min) 14 14 14 Hexanefeed rate(ml/min) 90 90 90 Polymerization temperature (° C.) 130 125 110Viscosity (cps) @190° C. 1132 2220 328CatalystA = dimethylsilyl (tetramethylcyclopentadienyl) (cyclododecylamido)titanium dimethylB = rac-dimethylsilyl bis(2-methyl-4-phenylindenyl) zirconium dimethyl

Several samples from the preceding experiments were analyzed todetermine their level of branching. For the purposes of this invention,the degree of branching is determined using the value of branching indexg′ at the molecular weight of Mz of the branched polymer. The resultsare presented in Tables 1 to 13.

Samples described in Example 4 and Examples 31-34 were fractionatedusing solvent extraction. The results are presented in Table 16.Selected fractionated fractions were analyzed using GPC-DRI-VIS-LS andDSC. The results from these analyses are also presented in Table 17. Thecomplex viscosity profiles of the fractionated fraction from sampledescribed in Example 31 were measured over the temperature range of 80to 130° C., are shown in FIG. 5.

The sample described in Example 4 and its fractions extracted fromsolvent extraction were analyzed using ¹³C NMR.

Percent mm triad is measured directly from the C-13 NMR spectrum; it isassumed that the level of mm triad in the mixture depends only on theamounts of aPP and scPP (“atactic polypropylene and semi-crystallinepolypropylene, respectively”) components in the sample. By knowing thetacticity (mm) level of the pure aPP and scPP components the proportionof each can be calculated that corresponds to the observed mm level inthe mixture. The values shown below show the percentage of isotatictriads on a whole, unfractionated polymer as well as the threefractions. The calculated data are generated by using the assumptionthat the isotactic and atactic reference polymers are indicative of thetacticities that are in the blocky polymer segments. Using the methyltriad region it is calculated that the isotactic reference polymer has94.7% mm and the atactic reference contains 13.6%. Sample % mm %Calculated Isotactic Polymer Unfractionated Polymer 68 66 Hexane Soluble16 around 2% Heptane Soluble 76 76 Heptane Insoluble 89 93

TABLE 16 Example Example Example Example Samples 31 33 32 34 Hexane room29.17 42.52 55.39 74.4 temperature solubles, wt. % Soxhlet hexane 25.1415.17 10.55 6.93 soluble, wt % Soxhlet heptane 7.88 7.1 8.53 0.44soluble, wt. % Soxhlet heptane 35.32 35 25.15 17.8 insoluble, wt. %

TABLE 17 Example 4 Hexane room Heptane Heptane temperature soxhletsoxhlet zebra solubles solubles insolubles Mn (kg/mol) 6.6 10.3 16.5 —Mw (kg/mol) 14.3 30.2 31.3 — Mz (kg/mol) 32.2 58.5 53.2 — g′ @Mz 1.160.86 0.87 — Tc (° C.) — 105.2 112.8 — Tm (° C.) — 138.2 145.2 — Tg (°C.) −11.1 — — — Heat of fusion (J/g) 0.0 68.6 108.9 — Example 31 Hexaneroom Soxhlet Soxhlet Soxhlet temperature hexane heptane heptane zebrasolubles solubles solubles insolubles Mn (kg/mol) 9.5 20.9 20.1 20.8 Mw(kg/mol) 12.7 48 56.3 47.4 Mz (kg/mol) 25 131.5 148.8 150.2 g′ @Mz 1.080.68 0.64 0.63 Tc (° C.) — 93.3 101.4 105.2 Tm (° C.) — 128.2 133.5138.3 Tg (° C.) −11.8 −8.3 — — Heat of fusion (J/g) 0.0 52.5 66.1 70.7

The viscosity of products of Examples 12, 22 and 49 were measured over atemperature range of 80 to 130° C. The complex viscosity profiles areshown in FIG. 1. These, data demonstrate the three-zone characteristicsdescribed above.

Selected samples and their blends were tested for adhesive performance.The pure polymers were compounded with tackifiers, oil or wax andstabilizer to form hot melt adhesive blends. The properties of thesepolymers and their blends were tested against typical commerciallyavailable EVA blends from Henkel and Chief. The blending was carried outunder low shear at elevated temperature to form fluid melts. The mixingtemperatures vary from about 130 to 190° C.

Escorez™ 5637 is a hydrogenated aromatic modified resin produced fromdicyclopentadiene feedstock, exhibiting a ring and ball softening pointof 130° C. available from ExxonMobil Chemical Company in Houston, Tex.

Paraflint H-1 is a Fisher-Tropsch wax exhibiting a molten viscosity of10 mPa sec at 250 F, available from Moore and Munger.

Aristowax 165 is a refined paraffin wax available from Frank B Ross Coin Jersey City N.J. It is isolated from petroleum and has a melt pointof 158 to 165 F.

Henkel Hot Melt 80-8368 is a commercial hot melt made from a blend ofEVA's, tackifiers, and wax available from Henkel Corp.

MAPP 40 is a maleic anhydridemodified polypropylene, having an acidnumber of 50, a viscosity of 300 cps at 190° C., a softening point of149° C., available from Chusei, USA.

Chief Hot Melt 268 is a commercial hot melt made from EVA, tackifiers,and wax available from Chief Adhesives.

KAYDOL® is a highly refined white mineral oil that consists of saturatedaliphatic and alicyclic non-polar hydrocarbons having a pour point of−20° C., having a kinematic viscosity of 64 to 70 cSt at 40° C.,available from Witco.

Licomont AR 504 is a maleic anhydride grafted polypropylene wax havingan acid number of 41, a viscosity of 373 mPas at 190° C., and asoftening point of 156° C. available from Clarient.

AC 540 is an ethylene acrylic acid copolymer having an acid number of40, a viscosity of 575 at 140° C. and a drop point of 105° C. availablefrom Honeywell.

Polywax 2000 is a Polyethylene wax available from Baker Petrolite PlainBOPP (biaxially oriented polypropylene film) a 28 micron thick film wasobtained from Mobil Films.

Corona treated BOPP (biaxially oriented polypropylene film) a 28 micronthick film was obtained from Mobil Films.

Paperboard 84A is gray Poster Board 20 pt chipboard with 20% recyclefiber available from Huckster packaging and supply, Inc. in Houston,Tex.

Paperboard 84B is generic poster board clay coated news print availablefrom Huckster packaging and supply, Inc. in Houston, Tex.

Cardboard 84C is generic corrugated cardboard 200 # stock available fromHuckster packaging and supply, Inc. in Houston, Tex. TradenameDescription Source Tackifiers Escorez ® 1102RM C5 tackifier ExxonMobilChemical Company Escorez ® 2203 is a low aromatic modified ExxonMobilChemical Company hydrocarbon resin having a narrow molecular weightdistribution produced from a feed of C5, C6 and C9 olefins and di-olefins, having a ring and ball softening point of about 95° C.Escorez ® 2393 is a highly aromatic modified ExxonMobil Chemical Companyhydrocarbon resin produced from a feed of C5, C6 and C9 olefins anddi-olefins, having a ring and ball softening point of about 93° C.Escorez ® 2596 is a low aromatic modified ExxonMobil Chemical Companyhydrocarbon resin having a broad molecular weight distribution producedfrom a feed of C5, C6 and C9 olefins and di-olefins, having a ring andball softening point of about 96° C. Escorez ® 5637 is a hydrogenatedaromatic ExxonMobil Chemical Company modified resin produced fromdicyclopentadiene feedstock, exhibiting a ring and ball softening pointof 130° C. Escorez ® 5690 is a hydrogenated aromatic ExxonMobil ChemicalCompany modified resin produced from dicyclopentadiene feedstock,exhibiting a ring and ball softening point of 130° C. Oils Primol 352Hydrogenated paraffinic oil ExxonMobil Chemical Company Primol 876Napthenic oils ExxonMobil Chemical Company Flexon 876 Napthenic oilsExxonMobil Chemical Company Kadol oil Refined white mineral oil WitcoPolymers/Adhesives Escorene UL 7720 Is an ethylene vinylacetateExxonMobil Chemical Company copolymer, having about 29 weight % vinylacetate and a melt index of 150 dg/min. NSC Easymelt Hot melt adhesivefor non-woven National Starch, Bound Brook, NJ applications. Henkel HotMelt 80-8368 Commercial adhesive of EVA, Henkel Corp tackifier, and waxChief Hot Melt 268 Commercial adhesive of EVA, Chief Adhesivestackifier, and wax Advantra 9250 Commercial adhesive of Fullerethylene/octene-1 metallocene polymers, tackifiers, and wax Tite BondWood Glue Water based adhesive Home Depot, Houston Texas Dap GlueSolvent based wood glue Home Depot, Houston Texas Waxes Aristowax 165Refined petroleum wax, melting Frank B Ross, Jersey City, NJtemperature: 158-165° F. AC 8 lot 500081EQ Polyethylene wax Honeywell,New Jersey Paraflint H-1 Fisher-Tropsch wax, 10 mPa @ Moore and Munger250° F. AR-504 Maleated PE wax acid number 41 Clarient and viscosity of373 mPa @ 190° C. AC-540 Ethylene acrylic acid copolymer Honeywell, NewJersey having an acid number of 40 and a viscosity of 575 cps @ 140° C.Polywax 2000 Polyethylene wax Baker Petrolite AC-1302P Maleatedpolypropylene Honeywell P-C80 Fischer Tropsch fractionated wax Moore andMunger MAPP-40 Maleic modified polypropylene Chusei, Pasadena Texas withacid number of 50, viscosity of 300 cps @ 190° C. Antioxidants and otheradditives Irganox 1010 Phenolic: antioxidant Ciba-Geigy Dolomite 16 meshsand Supplied by Fordamin Company Ltd (UK) Microcarb MC 50F calciumcarbonate Supplied by Microfine Minerals Ltd (UK) Glass beads of 3F typeGlass bead Supplied by Sovitec SA (Belgium) TiO2 Lot: TR92 titaniumdioxide Supplied by Hunstman Tioxide Ltd (UK) Test surfaces Metallizedacrylic coated Metallized acrylic coasted General Mills cardboard forcereal box Non-coated CB testliner 1250 gr/m2 for vegetable trays Kappa,Holland Paperboard 84A Gray poster 20 pt chipboard with HucksterPackaging and Supply, 20% recycle content Houston, TX Paperboard 84BGeneric posterboard clay coated Huckster Packaging and Supply, newsprintHouston, TX Paperboard 84C Generic corrugated cardboard HucksterPackaging and Supply, 200# stock Houston, TX Inland Paper Board HighPerformance box board Inland Paper Board and Packaging Company of RomeBlack White Fabric Printed stretch 100% Cotton with High FashionFabrics, Houston a Thread Count of 17 by 13 per Texas square cm, a moreloosely woven fabric Formica Tabs were made from standard Lowe'sHardware, Houston Texas sheet Formica Blue fabric Tabs were made fromBlue Stock High Fashion Fabrics, Houston 038COTP 100% Cotton, ThreadTexas. Count 21 by 45 per square cm with a weight of 0.022 grams persquare cm, a tightly woven cotton fabric Catalog paper Book paper boundby a hot melt Seton Catalog process as determined from examination NWCNon-woven Coverstock, Lohmann, Germany Paratherm PT 120/20 PEPolyethylene, White Opaque Tacolin Ltd, UK Micro-embossed CO/EX film(rubber treated inside), Reference #: CM001ARIE000757-C Polyester (PET)construct Polyester construct BOPP Bi-axially oriented polypropyleneMobil Films, Rochester, NY film, 28 micron Corona treated BOPP Coronatreated bi-axially oriented Mobil Films, Rochester, NY polypropylenefilm, 28 micron PP cast film construct A cast film.

REXTAC RT 2730 is a copolymer of propylene, butene and ethylene havingabout 67.5 mole percent propylene, about 30.5 mole percent butene andabout 2 mole percent ethylene produced by Huntsman, Company. Thecopolymer has about 15 mole percent BB dyads, 43 mole percent PB dyadsand about 43 mole percent PP dyads. The melting point is 70° C. with amelting range from 25 to 116° C. the Tg is −25° C., the crystallinity isabout 7 percent, the enthalpy is 10 J/g by DSC. The Mn is 8260 the Mw is59100 and the Mz 187900 by GPC. Mw/Mn is 7.15.

REXTAC RT 2715 is a copolymer of propylene, butene and ethylene havingabout 67.5 mole percent propylene, about 30.5 mole percent butene andabout 2 mole percent ethylene produced by Huntsman, Company. Thecopolymer has about 11 mole percent BB dyads, 40 mole percent PB dyadsand about 49 mole percent PP dyads. The melting point is 76° C. with amelting range form 23 to 124° C. the Tg is −22° C., the crystallinity isabout 7 percent, the enthalpy is 11 J/g by DSC. The Mn is 6630 the Mw is51200 and the Mz 166,700 by GPC. Mw/Mn is 7.7.

All the adhesive formulations are in weight percent, unless otherwisenoted in the compositions listed in Table 18 through Table 50. TABLE 18Applications Formulas (percent) and Performance Values Formulation A B CD E F Example 42 80 Escorez ™5637 7 7 13 10 10 Paraflint H-1 13 13 7 10Example 27 80 80 80 80 Aristowax 165 10 Henkel Standard 100 Hot Melt80-8368 Viscosity at 1091 870 1152 1000 945 700 190° C. (cps) SAFT, F (°C.) 233 253 257 253 259 182 (112) (123) (125) (123) (126) (83) Set Time(sec.) 1.5 1.5 2 1 2.5 1 Percent Substrate 0 80 95 10 100 100 Fiber TearLow Temperature −12° C., File folder

TABLE 19 Comparison of Blended aPP/scPP with branched aPP-g-scPPFormulation A B C D E F G Example 73 100 5 Example 74 100 39 Example 75100 39 Example 29 82 Irganox 1010 1 1 MAPP 40 5 5 Escorez ™ 5637 7 5Paraflint H-1 5 7 Henkel Standard 100 Hot Melt 80-8368 Chief Standard100 Hot Melt 268 Viscosity at 1132 2220 328 711 812 807 1055 190° C.(cps) SAFT, F (° C.) — — — 263 266 173 175 (128) (130) (78) (79) SetTime (sec.) >6 6 No 1.5-2.0 1.5 1 1.5 adhesion Percent Substrate 100 1000 100 85 100 100 Fiber Tear Low Temperature −12° C., cardboard PercentSubstrate 0 5 0 100 100 100 100 Fiber Tear Room Temperature 20-25° C.,File Folder

TABLE 20 Comparison of branched aPP-g-scPP with propylene/ethylenecopolymers Formulation A B C D E F G H I J K Example 41 100 90 90Example 16 100 90 90 C3/C2 100 90 90 Escorez 5637 7 3 7 3 7 3 ParaflintH-1 3 7 3 7 3 7 Henkel Standard 100 Hot Melt 80-8368 Chief Standard 100Hot Melt 268 SAFT, ° F. 204 195 193 215 198 200 198 199 179 171 185 SetTime (sec.) 6 5 2 >6 6 1.5 6 3 >6 2 1 Percent Substrate 0 100 0 100 1000 100 60 0 100 100 Fiber Tear Low Temperature −12° C., Filefolder

The C3/C2 is a comparative example. The polymer was anethylene/propylene copolymer with (ethylene content of about 10 wt. %.This polymer was made using rac-dimethylsilylbis(2-methyl-4-phenylindenyl)zirconium dimethyl at a polymerizationtemperature of 70 ° C., following the general procedure described abovefor example 1, except that only one catalyst was used. The polymer had apeak melting temperature of 95 ° C. and viscosity of 1368 cps at 190° C.TABLE 21 Multiple Polymer and Oil Blends of branched aPP-g-scPP PolymerFormulation A B C D E F G H I J Example 26 74 69 78  72  Example 25 7469 78  72  Example 23 5 9 5 9 Irganox 1010 1 1 1 1  1<  1<  1<  1<Kaydol Oil 10 10 10 10 5 9 5 9 Escorez ™5637 10 10 10 10 1 6 7 6Paraflint H-1 5 10 5 10 5 4 5 4 Henkel Standard 100 Hot Melt 80-8368Chief Standard 100 Hot Melt 268 Viscosity, cps 315 120 525 445 358  262 888  724  1002 732 190° C. SAFT, F (° C.) Set Time (sec.) 3 1.5 1.5 1  1.5   1.5 3 3 1.5 1.0 Percent Substrate 100 20 100 100 100  100  100 100  100 100 Fiber Tear Room Temperature 20-25° C., File Folder PercentSubstrate — — — — 100  100  100  100  100 100 Fiber Tear Low Temperature5° C., File folder

TABLE 22 Comparison of Various formulations of branched aPP-g-scPPFormulation A B C D E F G H I Example 25 92.5 78.6 78.6 Example 69 5 5Example 29 82 84.5 82 82 Escorez ™5400 5 7 AR 504 5 MAPP 40 5 5 2.5 5 5Irganox 1010 .5 .4 .4 1 1 1 1 Kaydol Oil 5 5 Escorez(tm) 5637 2 1.7 1.75 5 Paraflint H-1 5 4.3 4.3 7 7 7 5 Henkel Standard 100 Hot Melt 80-8368Chief Standard 100 Hot Melt 268 Viscosity at 790 695 688 688 758 750 830834 1050 190° C. (cps) SAFT, ° F. 263 >250 >250 265 266 265 265 184 171Set Time (sec.) 2.5 2 2 1.5 1.5 1.5 1.75 1 1.5 Percent Substrate 10 98100 75 60 90 100 100 100 Fiber Tear Low Temperature −12° C., cardboardPercent Substrate 34 100 100 100 100 100 100 100 100 Fiber Tear RoomTemperature 20-25° C., File Folder

TABLE 23 Hard and soft aPP-g-scPP mixes with Escorez(tm) 5400Formulation A B C D E F G H I Example 28 9 9 9 9 9 9 9 Example 17 78Example 40 78 Example 21 78 Example 20 78 Example 67 78 Example 25 78Example 26 78 Irganox 1010 1 1 1 1 1 1 1 Escorez ™5400 7 7 7 7 7 7 7Paraflint H-1 5 5 5 5 5 5 5 Henkel Standard 100 Hot Melt 80-8368 ChiefStandard 100 Hot Melt 268 Viscosity, cps 344 306 548 505 521 1185 404783 1090 190° C. SAFT, (° F.) Set Time (sec.) 3 3.5 3.5 2.5 1.5 >2 1.5 11.5 Percent Substrate 50 50 90 65 100 100 100 100 100 Fiber Tear LowTemperature 5° C., File Folder Percent Substrate 100 100 100 100 100 100100 100 100 Fiber Tear Room Temperature 20-25° C., File Folder Shore AHardness 74 77 54 63 76 76 76 80 85

There is no Table 24 TABLE 25 Comparison Various Wax Types with TwoPolymer Types Formulation A B C D E F G H I J K Paraflint H-1 0 10 0 0 00 10 0 0 Example 29 82 82 82 82 0 0 0 0 0 Example 62 82 82  82 82 82Escorez ™5637 7 7 7 7 7 7 7 7 7 Irganox 1010 1 1 1 1 1 1 1 1 1 AC 540 1010 5 Polywax 2000 10 10 5 Licowax PP 230 10 10  Henkel Standard 100 HotMelt 80-8368 Chief Standard 100 Hot Melt 268 Viscosity, cps 820 763 11401254 848 977  588 691 715 765 1131 190° C. Set Time (sec.) 0.5 1 4 2 1.5 4+ 1 0.5 1 1 1.5 Percent Substrate 0 0 95 50 70 100  0 0 50 100 100Fiber Tear Low Temperature −12° C., cardboard Percent Substrate 100 0 98100 100 100  0 5 100 100 100 Fiber Tear Room Temperature 20-25° C., FileFolder

TABLE 26 Formulating Response of butene-1 modified aPP-g-scPPFormulation A B C D E Example 68 100 93 Example 70 100 93 Escorez ™56372 2 Paraflint H-1 5 5 Henkel Standard 100 Hot Melt 80-8368 Viscosity @563 1100 485 1140 750 190° C. (cps) Set Time (sec.) 2.5 >3 1.5 2 1Percent Substrate 100 100 88 70 100 Fiber Tear Room Temperature 20-25°C., File Folder

TABLE 27 Comparison of dicyclopentadiene modified aPP-g-scPP with andwithout diene Formulation A B C D E F Example 28 93 100 80 Example 71100 93 Escorez ™ 5637 2 20 2 Paraflint H-1 5 5 Henkel Standard 100 HotMelt 80-8368 Viscosity, cps 390 661 205 524 502 — 190° C. Shore AHardness 22 34 45 — — — Set Time, sec 3 4 2.5 3.5 2 1 Percent Substrate50 80 90 80 90 90 Fiber Tear Room Temperature 20-25° C., File Folder

TABLE 28 Comparison Various aPP-g-scPP Polymer and Adhesive BlendsFormulation A B C D E F G H I J K Example 12 100 93 Example 24 100 93Example 22 100 93 88 Example 37 100 93 Escorez ™ 5637 2 2 2 4 2Paraflint H-1 5 5 5 8 5 Henkel Standard 100 Hot Melt 80-8368 ChiefStandard 100 Hot Melt 268 Viscosity, cps 813 875 2240 1527 1240 950 797568 497 730 1027 190° C. Set Time, sec 3 3 3 3 3.5 2.5 1.5 3.5 2.5 1 1.5Percent Substrate 85 95 95 95 90 90 90 90 95 90 10 Fiber Tear RoomTemperature 20-25° C., File Folder

TABLE 29 Example Adhesive Testing on a Variety of Surfaces FormulationBlend of 78% example 29, 5% Licomont AR504, 7% Escorez 5637, 5%Paraflint H-1, 5% Kaydol oil. 1% Irganox 1010 was added to the blendHenkel 80-8368 Hot Melt Maximum average Force Maximum average Force byDot T-Peel Test, Failure by Dot T-Peel Test Surface (Newtons\lbs) Type(Newtons\lbs) Failure Type Cardboard 84C 24.2\5.4  Substrate Failure16.4\3.7  Substrate Failure BOPP Film 19.2\4.3  Cohesive Failure 1.0\0.2Complex jerking (Corona Treated) PP Film plain 13.7\3.1  Several Types1.0\0.2 Complex jerking Paperboard 84B 6.0\1.3 Substrate Failure 5.3\1.2Substrate Failure Paperboard 84A 4.7\1.1 Substrate Failure 4.6\1.0Substrate Failure Aluminum foil 3.2\0.7 Cohesive Failure 1.3\0.3Cohesive Failure

Example EX1-EX13

The following samples were made at a temperature range of 70 to 125° C.,following the general procedure described above with the followingexceptions: (1) a small quantity of 1,9-decadiene was fed as thediolefin monomer in Example EX1-EX3, EX5 and EX9; (2) ethylene was usedin Example EX13-EX17. The detailed experimental conditions and resultsare presented in Tables 30, 31 and 32. TABLE 30 Example EX1 EX2 EX3 EX4EX5 EX6 Catalyst #1 A A A A A G Catalyst #1 5.22E−06 5.88E−06 6.10E−063.91E−06 1.82E−06 9.89E−07 feed rate (mole/min) Catalyst #2 B E B C B CCatalyst #2 7.65E−07 2.62E−06 2.83E−07 9.86E−07 9.45E−08 2.22E−07 feedrate (mole/min) Propylene feed 14 14 14 14 14 14 rate (g/min) 1,9decadiene 0.09 0.10 0.19 0.00 0.01 0.00 feed rate (ml/min) H2 (cc/min) 00 30 0 0 0 Hexane feed 90 90 90 90 90 90 rate (ml/min) Polymerization 9575 70 92 100 105 temperature (° C.) Mn (kg/mol) 28.1 — 15.8 — 33 — Mw(kg/mol) 63 — 58.3 — 67.7 — Mz (kg/mol) 168.3 — 203.7 — 136.4 — g′ @ Mz0.81 — 0.78 — — — Tc (° C.) 100.7 74.8 91.9 54.6 86.4 60.1 Tm (° C.)146.1 113.8 148.9 103.0 149.4 102.9 Tg (° C.) −7.6 −8.2 −7.1 −8.3 −6.7−8.2 Heat of fusion 36.5 27.8 19.3 23.9 12.5 35.8 (J/g) Viscosity 112004940 10100 2940 54870 5340 @ 190° C. (cps)CatalystsA = dimethylsilyl (tetramethylcyclopentadienyl)(cyclododecylamido)titanium dimethylB = rac-dimethylsilyl bis(2-methyl-4-phenylindenyl) zirconium dimethylC = rac-dimethylsilyl bis (indenyl) hafnium dimethylE = rac-dimethylsily bis(2-methylindenyl)zirconium dimethylG =di(p-triethylsilylphenyl)methylene](cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdimethyl

TABLE 31 Example EX7 EX8 EX9 EX10 EX11 EX12 EX13 Catalyst #1 G G G G G GG Catalyst #1 1.65E−06 1.65E−06 1.77E−06 2.35E−06 1.65E−06 9.89E−071.77E−06 feed rate (mole/min) Catalyst #2 B B B B B C B Catalyst #27.09E−08 4.72E−08 1.42E−07 5.74E−08 7.09E−08 3.70E−07 1.42E−07 feed rate(mole/min) Propylene feed 14 14 14 14 14 14 14 rate (g/min) Ethylenefeed — — — — — — 0.2 rate (SLPM) 1,9 decadiene — — 0.02 — — — — feedrate (ml/min) Hexane feed 90 90 90 90 90 90 90 rate (ml/min)Polymerization 110 115 125 130 120 105 110 temperature (° C.) Mn(kg/mol) 22.5 — 17.7 — — — — Mw (kg/mol) 68.6 — 35.9 — — — — Mz (kg/mol)132.4 — 67.8 — — — — g′ @ Mz — — 0.82 — — — — Tc (° C.) 96.0 81.6 82.581.0 96.5 54.2 56.9 Tm (° C.) 147.9 142.6 124.9 134.1 144.7 94.5 113.5Tg (° C.) −3.3 −2.8 −6.3 −3.9 −4.2 −10.5 −9.6 Heat of fusion 40.7 15.237.2 17.1 40.0 32.7 21.7 (J/g) Viscosity 45400 47500 1180 8325 7957 11577975 @ 190° C. (cps)CatalystsB = rac-dimethylsilyl bis(2-methyl-4-phenylindenyl) zirconium dimethylC = rac-dimethylsilyl bis (indenyl) hafnium dimethylG =di(p-triethylsilylphenyl)methylene](cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdimethyl

TABLE 32 Example EX14 EX15 EX16 EX17 Catalyst #1 G G G G Catalyst #11.77E−06 1.77E−06 1.77E−06 1.77E−06 feed rate (mole/min) Catalyst #2 B BB B Catalyst #2 3.12E−07 3.12E−07 3.12E−07 3.12E−07 feed rate (mole/min)Propylene feed 14 14 10 10 rate (g/min) Ethylene feed 1.5 0.8 0.8 1.5rate (SLPM) Hexane feed 90 90 90 90 rate (ml/min) Polymerization 80 80105 105 temperature (° C.) Mn (kg/mol) Mw (kg/mol) Mz (kg/mol) g′ @ MzTc (° C.) 28.7 58.0 19.1 — Tm (° C.) 73.7 99.3 57.6 −47.8 Tg (° C.)−26.3 −19.4 −26.8 −19.5 Heat of fusion 14.8 29.6 8.0 3.7 (J/g) Viscosity@ 23400 37120 495 481 190° C. (cps) Ethylene content 16.9 10.7 (mole %)CatalystsB = rac-dimethylsilyl bis(2-methyl-4-phenylindenyl) zirconium dimethylG =di(p-triethylsilylphenyl)methylene](cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdimethylPolymerization Conditions

Propylene feed at the rate of 8 lb/hr was combined with hexane at 17lb/hr to form 25 lb/hr of reactor feed solution. Tri-n-octyl aluminum(TNOA) as a 3 wt. % solution in hexane (obtained from Albemarle) wasintroduced into this stream at the rate of 0.0006 lb/hr.

Catalyst and activator entered the reactor from a separate port. Thecatalyst solution consisted of a mixture ofdi(p-triethylsilylphenyl)methylene](cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdimethyl (catalyst G) and rac-dimethylsilylbis(2-methyl-4-phenylindenyl) zirconium dimethyl (catalyst B), with 97molar % of catalyst G. The catalyst solution was prepared by dissolvingthe catalyst mixture in toluene to form a 0.5 wt % solution. Theactivator feed stream was made up of a 0.2 wt-% solution ofN,N-dimethylanilinium tetrakis(pentafluorophenyl) borate in toluene.Both the catalysts and activator were obtained from Albemarle. Thecatalyst and activator feed lines were configured to mix in lineimmediately upstream of the reactor, with an estimated contact time of2-4~ minutes. The catalyst and activator feed rates were 0.04 g/hr and0.1 g/hr respectively.

The reactor feed was converted to polymer through two continuous stirredtank reactors in series. The temperatures of both reactors werecontrolled at 135° C. The reactors were operated liquid full under 530psig pressure. The residence time of the feed in each reactor was 45minutes. Conversion of propylene to polymer product was about 91%.

Molten polymer was recovered from solution via two flash stages, eachwith a preheater. The first stage (20 psig) polymer contained about 2%solvent and the second stage (50 torr vacuum) incorporated about 800 ppmvolatiles. Water was injected into the second stage flash(devolatilizer) feed to quench residual catalyst and aid with solventstripping. The properties of the polymer and the finished adhesives aresummarized in Table 33. TABLE 33 Example # PP1 PP2 PP3 PP4 PP5 PP6 PP7PP8 Polymerization 132 135 135 135 135 134 133 137 temperature (° C.)Cat1 in catalyst 96 93 93 93 93 93 96 93 blend (mol %) Catalyst in 3.204.17 4.17 4.17 4.17 4.17 4.17 3.8 reactor feed (wppm) Propylene in 28.0029.17 29.17 29.17 29.17 28.0 28.0 30.0 reactor feed (wt %) Scavenger(wppm) 7.44 25 25 25 25 24 24 24 Quench water 1.82 0.86 0.86 0.86 0.621.4 2.8 0 (wt %) Mn (kg/mol) 18.3 17.1 13 16.7 12.3 11.4 17.3 18.5 Mw(kg/mol) 41.7 36.6 32.5 34.4 32.3 31.9 38.5 34.1 Mz (kg/mol) 76.4 68.161.9 61.7 64.6 61.6 71.4 69.6 g′ @Mz — 0.83 0.85 0.83 0.81 0.83 0.940.89 Tc (° C.) 69.2 79.8 80.6 78.4 63.8 71.8 62.8 85 Tm (° C.) 131 134136 137 130 132 137 136 Heat of fusion 15.9 25.7 30.7 28.7 38 28.2 9.538.6 (J/g) Viscosity 2300 1992 1382 1527 1211 1340 4235 1270 @ 190° C.(cps)CatalystB = rac-dimethylsilyl bis(2-methyl-4-phenylindenyl) zirconium dimethylG =di(p-triethylsilylphenyl)methylene](cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdimethyl

All documents described herein are incorporated by reference herein,including any priority documents and/or testing procedures. As isapparent from the foregoing general description and the specificembodiments, while forms of the invention have been illustrated anddescribed, various modifications can be made without departing from thespirit and scope of the invention. Accordingly, it is not intended thatthe invention be limited thereby.

1. A polymer comprising at least 50 mol % of one or more C3 to C40olefins where the polymer has: a) a Dot T-Peel of 1 Newton or more onKraft paper; b) an Mw of 10,000 to 100,000; c) a branching index (g′) offrom 0.4 to 0.98 measured at the Mz of the polymer when the polymer hasan Mw of 10,000 to 60,000, or a branching index (g′) of from 0.4 to 0.95measured at the Mz of the polymer when the polymer has an Mw of 10,000to 100,000; d) a heat of fusion of 1 to 70 J/g; and e) a heptaneinsoluble fraction of 70 weight % or less, based upon the weight of thepolymer, where the heptane insoluble fraction has branching index g′ of0.9 or less as measured at the Mz of the polymer.
 2. The polymer ofclaim 1 wherein the polymer has: a) a Dot T-Peel of 2 Newton or more onKraft paper; b) a branching index (g′) of from 0.4 to 0.98 measured atthe Mz of the polymer; c) a Mw of 10,000 to 60,000; and d) a heat offusion of 1 to) 50 J/g.
 3. The polymer of claim 1 where the polymer is ahomopolypropylene or a copolymer of propylene and up to 5 mole %ethylene having: a) an isotactic run length of 1 to 30, b) a percent ofr dyad of greater than 20%, and c) a heat of fusion of between 1 and 50J/g.
 4. The polymer of claim 1 wherein the polymer comprises propyleneand less than 15 mole % of ethylene.
 5. The polymer of claim 1 whereinthe polymer has a melt viscosity of 7000 mPa·sec or less at 190° C. 6.The polymer of claim 1 wherein the polymer has a melt viscosity of 5000mPa·sec or less at 190° C.
 7. The polymer of claim 1 wherein the polymerhas a melt viscosity of between 250 and 6000 mPa·sec at 190° C.
 8. Thepolymer of claim 1 wherein the polymer has a melt viscosity of between500 and 3000 mPa·sec at 190° C.
 9. The polymer of claim 4 wherein thepolymer has a Tg of 0° C. or less.
 10. The polymer of claim 4 whereinthe polymer has a Tg of −10° C. or less.
 11. The polymer of claim 1wherein the polymer has an Mw of 10,000 to 75,000 and a branching indexof from 0.4 to 0.6.
 12. The polymer of claim 1 wherein the polymer hasan Mw of 10,000 to 50,000 and a branching index of from 0.4 to 0.7. 13.The polymer of claim 1 wherein the polymer has an Mw of 10,000 to 30,000and a branching index of from 0.4 to 0.98.
 14. The polymer of claim 1wherein the polymer has a branching index (g′) of from 0.4 to 0.90measured at the Mz of the polymer.
 15. The polymer of claim 1 whereinthe SEC graph of the polymer is bi- or multi-modal.
 16. The polymer ofclaim 1 wherein the polymer has a precent crystallinity of from 5 to 40%and an amorphous content of at least 60%.
 17. The polymer of claim 1wherein the polymer has a) a peak melting point between 60 and 190° C.;b) a heat of fusion of 1 to 70 J/g; and c) a melt viscosity of 8000mPa·sec or less at 190° C.
 18. The polymer of claim 1 wherein thepolymer has: a) a Tg of −10° C. or less; b) a melt viscosity between2000 and 6000 mPa·sec; c) a molecular weight distribution (Mw/Mn) of atleast 5; and d) a bi- or multi-modal SEC graph of the polymer.
 19. Thepolymer of claim 1 wherein the polymer has a crystallinity between 10and 30%.
 20. The polymer of claim 1 wherein the polymer has 20 wt. % ormore of hexane room temperature soluble fraction and 50 wt % or less ofSoxhlet heptane insolubles.
 21. The polymer of claim 1 wherein thepolymer comprises less than 3.0 mole % ethylene.
 22. The polymer ofclaim 1 wherein the polymer comprises less than 1.0 mole % ethylene. 23.The composition of claim 1 wherein the composition has a branching index(g′) of from 0.4 to 0.90 measured at the Mz of the polymer.
 24. Thecomposition of claim 1 wherein the composition has a branching index(g′) of from 0.4 to 0.85 measured at the Mz of the polymer.
 25. Thecomposition of claim 1 wherein the composition has a branching index(g′) of from 0.4 to 0.80 measured at the Mz of the polymer.
 26. Thepolymer of claim 1 further comprising diolefin.
 27. The polymer of claim26 wherein the diolefin comprises one or more C4 to C40 diolefins. 28.The polymer of claim 26 wherein the diolefin is selected from the groupconsisting of 1,6-heptadiene, 1,7-octadiene, 1,8-nonadiene,1,9-decadiene, 1,10-undecadiene, 1,11-dodecadiene, 1,12-tridecadiene,1,13-tetradecadiene, cyclopentadiene, vinylnorbornene, norbornadiene,ethylidene norbornene, divinylbenzene, dicyclopentadiene, polybutadieneshaving an Mw less than 1000 g/mol, or combinations thereof.
 29. Thepolymer of claim 1 wherein the polymer has an Mz/Mn of 2 to
 200. 30. Thepolymer of claim 1 wherein the polymer has an Mz of 15,000 to 500,000.31. The polymer of claim 1 wherein the polymer has a SAFT of 50 to 150°C.
 32. The polymer of claim 1 wherein the polymer has a Shore A hardnessof 95 or less.
 33. The polymer of claim 1 wherein the polymer has a settime of 5 seconds or less.
 34. The polymer of claim 1 wherein thepolymer has an Mw/Mn of 2 to
 75. 35. A continuous process to produce abranched olefin polymer comprising: 1) selecting a first catalystcomponent capable of producing a polymer having an Mw of 100,000 or lessand a crystallinity of 5% or less under selected polymerizationconditions; 2) selecting a second catalyst component capable ofproducing polymer having an Mw of 100,000 or less and a crystallinity of20% or more at the selected polymerization conditions; 3) contacting thecatalyst components in the presence of one or more activators with oneor more C3 to C40 olefins; and, 4) at a temperature of greater than 100°C.; 5) at a residence time of 1.20 minutes or less; 6) wherein the ratioof the first catalyst to the second catalyst is from 1:1 to 50:1; 7)wherein the activity of the catalyst components is at least 50 kilogramsof polymer per gram of the catalyst compounds; and wherein at least 80%of the olefins are converted to polymer; and 8) obtaining a polymercomprising at least 50 mol % of the C3 to C40 olefins where the polymerhas: a) a Dot T-Peel of 1 Newton or more on Kraft paper; b) an Mw of10,000 to 100,000; c) a branching index (g′) of from 0.4 to 0.98measured at the Mz of the polymer when the polymer has an Mw of 10,000to 60,000, or a branching index (g′) of from 0.4 to 0.95 measured at theMz of the polymer when the polymer has an Mw of 10,000 to 100,000; d) aheat of fusion of 1 to ′70 J/g; and e) a heptane insoluble fraction 70weight % or less, based upon the weight of the polymer, and the heptaneinsoluble fraction has branching index g′ of 0.9 or less as measured atthe Mz of the polymer.
 36. The process of claim 35 wherein the olefincomprises propylene.
 37. The process of claim 35 wherein the firstcatalyst component comprises a non-stereospecific metallocene catalystcompound.
 38. The process of claim 35 wherein the first catalystcomponent comprises a stereospecific metallocene catalyst compound. 39.The process of claim 35 wherein the second catalyst component comprisesa stereospecific metallocene catalyst compound.
 40. The process of claim35 wherein the first catalyst component comprises one or more of:dimethylsilyl(tetramethylcyclopentadienyl)(cyclododecylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(cyclohexyl-amido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(1-adamantylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(t-butylamido)titaniumdichloride,dimethylsilyl(tetramethylcyclopentadienyl)(s-butylamido)titaniumdichloride, ordimethylsilyl(tetramethylcyclopentadienyl)(n-butylamido)titaniumdichloride.
 41. The process of claim 35 wherein the second catalystcomponent comprises one or more of the racemic versions of:dimethylsilyl(2-methyl-4-phenylindenyl)zirconium dichloride,dimethylsilyl(2-methyl-4-phenylindenyl)zirconium dimethyl,dimethylsilyl(2-methyl-4-phenylindenyl)hafnium dichloride,dimethylsilyl(2-methyl-4-phenylindenyl)hafnium dimethyl, dimethylsilylbis(indenyl)hafnium dimethyl, dimethylsilyl bis(indenyl)hafniumdichloride, dimethylsilyl bis(indenyl)zirconium dimethyl, dimethylsilylbis(indenyl)zirconium dichloride, the racemic isomers of:dimethylsilanediylbis(2-methylindenyl)metal dichloride;dimethylsilanediylbis(indenyl)metal dichloride;dimethylsilanediylbis(indenyl)metal dimethyl;dimethylsilanediylbis(tetrahydroindenyl)metal dichloride;dimethylsilanediylbis(tetrahydroindenyl)metal dimethyl;dimethylsilanediylbis(indenyl)metal diethyl; anddibenzylsilanediylbis(indenyl)metal dimethyl; wherein the metal can bechosen from Zr, Hf, or Ti.
 42. The process of claim 35 wherein theactivator comprises an alumoxane.
 43. The process of claim 35 whereinthe activator comprises an ionizing compound.
 44. The process of claim35 wherein the activator comprises a non-coordinating anion.
 45. Theprocess of claim 35 wherein the activator comprises one or more ofmethylalumoxane, trimethylammonium tetraphenylborate, triethylammoniumtetraphenylborate, tripropylammonium tetraphenylborate,tri(n-butyl)ammonium tetraphenylborate, tri(t-butyl)ammoniumtetraphenylborate, N,N-dimethylanilinium tetraphenylborate,N,N-diethylanilinium tetraphenylborate,N,N-dimethyl-(2,4,6-trimethylanilinium)tetraphenylborate,trimethylammonium tetrakis(pentafluorophenyl)borate, triethylammoniumtetrakis(peintafluorophenyl)borate, tripropylammoniumtetrakis(pentafluorophenyl)borate, tri(n-butyl)ammoniumtetrakis(pentafluorophenyl)borate, tri(sec-butyl)ammoniumtetrakis(pentafluorophenyl)borate, N,N-dimethylaniliniumtetrakis(pentafluorophenyl)borate, N,N-diethylaniliniumtetrakis(pentafluorophenyl) borate,N,N-dimethyl-(2,4,6-trimethylanilinium)tetrakis(pentafluorophenyl)borate,trimethylammonium tetrakis-(2,3,4,6-tetrafluorophenylborate,triethylammonium tetrakis-(2,3,4,6-tetrafluorophenyl)borate,tripropylammonium tetrakis-(2,3,4,6-tetrafluorophenyl)borate,tri(n-butyl)ammonium tetrakis-(2,3,4,6-tetrafluoro-phenyl)borate,dimethyl(t-butyl)ammonium tetrakis-(2,3,4,6-tetrafluorophenyl)borate,N,N-dimethylanilinium tetrakis-(2,3,4,6-tetrafluorophenyl) borate,N,N-diethylanilinium tetrakis-(2,3,4,6-tetrafluorophenyl) borate, andN,N-dimethyl-(2,4,6-trimethylanilinium)tetrakis-(2,3,4,6-tetrafluorophenyl)borate;di-(i-propyl)ammonium tetrakis(pentafluorophenyl)borate;dicyclohexylammonium tetrakis(pentafluorophenyl)borate;triphenylphosphonium tetrakis(pentafluorophenyl)borate;tri(o-tolyl)phosphonium tetrakis(pentafluorophenyl) borate; andtri(2,6-dimethylphenyl)phosphonium tetrakis(pentafluorophenyl)borate.46. The process of claim 35 wherein the first catalyst component iscapable of polymerizing macromonomers having reactive termini; and thesecond component is capable of producing macromonomers having reactivetermini.
 47. The process of claim 35 wherein the first catalystcomponent comprises one or more ofdi(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconiumdichloride,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafniumdichloride, di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)zirconium dimethyl,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,8-di-t-butylfluorenyl)hafnium dimethyl,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconium dichloride,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdichloride,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)zirconiumdimethyl,di(p-triethylsilylphenyl)methylene(cyclopentadienyl)(3,3,6,6,9,9,12,12-octamethyl-4,4,5,5,8,8,9,9-octahydrodibenzyl[b,h]fluorenyl)hafniumdimethyl, and the meso forms of: dimethylsilylbis(indenyl) zirconiumdichloride, dimethylsilylbis(indenyl)zirconium dimethyl,ethylenebis(indenyl)zirconium dichloride, ethylenebis(indenyl)zirconiumdimethyl, dimethylsilylbis(indenyl)hafnium dichloride,dimethylsilylbis(indenyl)hafnium dimethyl, ethylenebis(indenyl)hafniumdichloride, ethylenebis(indenyl)hafnium dimethyl,dimethylsilylbis(tetrahydroindenyl)zirconium dichloride,dimethylsilylbis(tetrahydroindenyl)zirconium dimethyl,ethylenebis(tetrahydroindenyl)zirconium dichloride,ethylenebis(tetrahydroindenyl)zirconium dimethyl,dimethylsilylbis(tetrahydroindenyl)hafnium dichloride,dimethylsilylbis(tetrahydroindenyl)hafnium dimethyl,ethylenebis(tetrahydroindenyl)hafnium dichloride,ethylenebis(tetrahydroindenyl)hafnium dimethyl,dimethylsilylbis(2-methylindenyl)zirconium dichloride,dimethylsilylbis(2-methylindenyl)zirconium dimethyl,ethylenebis(2-methylindenyl)zirconium dichloride,ethylenebis(2-methylindenyl)zirconium dimethyl,dimethylsilylbis(2-methylindenyl)hafnium dichloride,dimethylsilylbis(2-methylindenyl)hafnium dimethyl,ethylenebis(2-methylindenyl)hafnium dichloride, andethylenebis(2-methylindenyl)hafnium dimethyl.
 48. The process of claim35 wherein the monomers comprise propylene and butene.
 49. The processof claim 35 further comprising diolefin.
 50. The process of claim 49wherein the diolefin comprises one or more C4 to C40 diolefins.
 51. Theprocess of claim 50 wherein the wherein the diolefin is selected fromthe group consisting of 1,6-heptadiene, 1,7-octadiene, 1,8-nonadiene,1,9-decadiene, 1,10-undecadiene, ′1,11-dodecadiene, 1,12-tridecadiene,1,13-tetradecadiene, cyclopentadiene, vinylnorbornene, norbornadiene,ethylidene norbornene, divinylbenzene, dicyclopentadiene, polybutadieneshaving an Mw less than 1000 g/mol, or combinations thereof.
 52. Theprocess of claim 49 further comprising one or more dienes selected fromthe group consisting of 1,6-heptadiene, 1,7-octadiene, 1,8-nonadiene,1,9-decadiene, 1,10-undecadiene, 1,11-dodecadiene, 1,12-tridecadiene,1,13-tetradecadiene, cyclopentadiene, vinylnorbomene, norbornadiene,ethylidene norbornene, divinylbenzene, dicyclopentadiene, polybutadieneshaving an Mw less than 1000 g/mol, or combinations thereof.
 53. Theprocess of claim 35 wherein the reaction zone is a gas phase reactor.54. The process of claim 35 wherein the reaction zone is a solutionphase reactor.
 55. The process of claim 35 wherein the reaction zone isa slurry phase reactor.
 56. The process of claim 36 wherein the reactionzone is a solution phase reactor.
 57. A composition comprising ahomopolymer of propylene and or a copolymer of propylene and one or moreof butene, pentene, hexene, octene, nonene, and decene, wherein thecopolymer comprises less than 50 mole % ethylene, and wherein thehomopolymer or copolymer has a Dot T-Peel of 3 or more Newtons; aviscosity of 8000 mPa·sec or less at 190° C.; a branching index (g′) offrom 0.4 to 0.85 measured at the Mz of the polymer; an Mw of 100,000 orless; a heat of fusion of 1 to 70 J/g; and a heptane insoluble fraction70 weight % or less, based upon the weight of the polymer, and theheptane insoluble fraction has branching index g′ of 0.9 or less asmeasured at the Mz of the polymer.
 58. A composition comprising a.polymer of propylene, having from 0 to 5 mol % ethylene and from 0 to 40mol % of a C5 to C12 olefin, and 0 to 10 mol % of a diene where thepolymer has: a) a Dot T-Peel of 1 Newton or more; and b) an Mw of100,000 or less; and c) a Mz/Mn of 2-200; and d) an Mw of 100,000 orless and a branching index of from 0.4 to 0.5, or an Mw of 75,000 orless and a branching index of from 0.4 to 0.6, or an Mw of 50,000 orless and a branching index of from 0.4 to 0.7, or an Mw of 30,000 orless and a branching index of from 0.4 to 0.98; and d) a peak meltingpoint between 60 and 190° C., and e) a viscosity of 8000 mPa·sec or lessat 190° C.; and f) a heat of fusion from 1 to 70 J/g; and g) a Shore AHardness (as measured by ASTM 2240) of 70 or less; and h) A ShearAdhesion Fail Temperature 40 to 150° C.; and i) a set time of 5 secondsor less; and j) an Mw/Mn of 3 to 75; and k) an Mz of 20,000 to 500,000;and l) a melt index of 900 dg/min or less; and m) a heptane insolublefraction of 70 weight % or less, based upon the weight of the polymer,where the heptane insoluble fraction has branching index g′ of 0.9 orless as measured at the Mz of the polymer.
 59. A polymer comprising oneor more C3 to C40 olefins, optionally one or more diolefins, and lessthan 1 mole % of ethylene where the polymer has: a) a Dot T-Peel of INewton or more; and b) a branching index (g′) of from 0.4 to 0.95measured at the Mz of the polymer; and c) an Mw of 100,000 or less; andd) at least 2 mol % (CH₂)₂ units; and e) a heat of fusion of 1 to 70J/g; and f) a heptane insoluble fraction of 70 weight % or less, basedupon the weight of the polymer, where the heptane insoluble fraction hasbranching index g′ of 0.9 or less as measured at the Mz of the polymer.60. A polymer comprising one or more C3 to C40 olefins, optionally oneor more diolefins, and less than 50 mole % of ethylene where the polymerhas: a) a Dot T-Peel of 5 Newton or more ; and b) a branching index (g′)of from 0.4 to 0.95 measured at the Mz of the polymer; and c) an Mw of100,000 or less; and d) a heat of fusion of 1 to 70 J/g; and e) aheptane insoluble fraction 70 weight % or less, based upon the weight ofthe polymer, and the heptane insoluble fraction has branching index g′of 0.9 or less as measured at the Mz of the polymer.
 61. A pelletcomprising the polymer of claim 1.